US11542668B2 - Sterol additive in asphalt pavement - Google Patents

Sterol additive in asphalt pavement Download PDF

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Publication number
US11542668B2
US11542668B2 US15/886,605 US201815886605A US11542668B2 US 11542668 B2 US11542668 B2 US 11542668B2 US 201815886605 A US201815886605 A US 201815886605A US 11542668 B2 US11542668 B2 US 11542668B2
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United States
Prior art keywords
asphalt
sterol
binder
pavement
asphalt binder
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US15/886,605
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US20180215919A1 (en
Inventor
Gerald H. Reinke
Gaylon L. Baumgardner
Andrew Hanz
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ALM Holding Co
Ergon Asphalt and Emulsions Inc
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ALM Holding Co
Ergon Asphalt and Emulsions Inc
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Application filed by ALM Holding Co, Ergon Asphalt and Emulsions Inc filed Critical ALM Holding Co
Priority to US15/886,605 priority Critical patent/US11542668B2/en
Publication of US20180215919A1 publication Critical patent/US20180215919A1/en
Priority to PCT/US2018/055443 priority patent/WO2019079101A1/en
Priority to CA3079097A priority patent/CA3079097A1/en
Priority to MX2020003711A priority patent/MX2020003711A/en
Priority to AU2018350814A priority patent/AU2018350814A1/en
Priority to CR20200164A priority patent/CR20200164A/en
Priority to BR112020007768-2A priority patent/BR112020007768A2/en
Priority to CN201880083286.0A priority patent/CN111902487A/en
Priority to US16/757,697 priority patent/US11718756B2/en
Priority to JP2020522056A priority patent/JP2021500496A/en
Priority to EP18795903.6A priority patent/EP3697849A1/en
Priority to ZA2020/02127A priority patent/ZA202002127B/en
Assigned to A.L.M. HOLDING COMPANY, ERGON ASPHALT & EMULSIONS, INC. reassignment A.L.M. HOLDING COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: BAUMGARDNER, GAYLON L., HANZ, Andrew, REINKE, GERALD H.
Priority to US18/086,231 priority patent/US20230128467A1/en
Application granted granted Critical
Publication of US11542668B2 publication Critical patent/US11542668B2/en
Priority to US18/209,922 priority patent/US20230323126A1/en
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    • EFIXED CONSTRUCTIONS
    • E01CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01CCONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C11/00Details of pavings
    • E01C11/005Methods or materials for repairing pavings
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B18/00Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
    • C04B18/04Waste materials; Refuse
    • C04B18/16Waste materials; Refuse from building or ceramic industry
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/02Alcohols; Phenols; Ethers
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/24Macromolecular compounds
    • C04B24/34Natural resins, e.g. rosin
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B26/00Compositions of mortars, concrete or artificial stone, containing only organic binders, e.g. polymer or resin concrete
    • C04B26/02Macromolecular compounds
    • C04B26/26Bituminous materials, e.g. tar, pitch
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B40/00Processes, in general, for influencing or modifying the properties of mortars, concrete or artificial stone compositions, e.g. their setting or hardening ability
    • C04B40/0082Processes, in general, for influencing or modifying the properties of mortars, concrete or artificial stone compositions, e.g. their setting or hardening ability making use of a rise in temperature, e.g. caused by an exothermic reaction
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/04Oxygen-containing compounds
    • C08K5/05Alcohols; Metal alcoholates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L91/00Compositions of oils, fats or waxes; Compositions of derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L95/00Compositions of bituminous materials, e.g. asphalt, tar, pitch
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L95/00Compositions of bituminous materials, e.g. asphalt, tar, pitch
    • C08L95/005Aqueous compositions, e.g. emulsions
    • EFIXED CONSTRUCTIONS
    • E01CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01CCONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C7/00Coherent pavings made in situ
    • E01C7/08Coherent pavings made in situ made of road-metal and binders
    • E01C7/35Toppings or surface dressings; Methods of mixing, impregnating, or spreading them
    • E01C7/353Toppings or surface dressings; Methods of mixing, impregnating, or spreading them with exclusively bituminous binders; Aggregate, fillers or other additives for application on or in the surface of toppings with exclusively bituminous binders, e.g. for roughening or clearing
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00474Uses not provided for elsewhere in C04B2111/00
    • C04B2111/00612Uses not provided for elsewhere in C04B2111/00 as one or more layers of a layered structure
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00474Uses not provided for elsewhere in C04B2111/00
    • C04B2111/0075Uses not provided for elsewhere in C04B2111/00 for road construction
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2207/00Properties characterising the ingredient of the composition
    • C08L2207/20Recycled plastic
    • C08L2207/22Recycled asphalt
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2555/00Characteristics of bituminous mixtures
    • C08L2555/20Mixtures of bitumen and aggregate defined by their production temperatures, e.g. production of asphalt for road or pavement applications
    • C08L2555/28Asphalt produced between 0°C and below 65°C, e.g. cold mix asphalt produced between 0°C and 35°C
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2555/00Characteristics of bituminous mixtures
    • C08L2555/30Environmental or health characteristics, e.g. energy consumption, recycling or safety issues
    • C08L2555/34Recycled or waste materials, e.g. reclaimed bitumen, asphalt, roads or pathways, recycled roof coverings or shingles, recycled aggregate, recycled tires, crumb rubber, glass or cullet, fly or fuel ash, or slag
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2555/00Characteristics of bituminous mixtures
    • C08L2555/40Mixtures based upon bitumen or asphalt containing functional additives
    • C08L2555/60Organic non-macromolecular ingredients, e.g. oil, fat, wax or natural dye
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

Definitions

  • Asphalt pavement is a composite material that is a mixture of mineral aggregate and a liquefied asphalt (bitumen) binder, which hardens to form a robust surface.
  • the bitumen is generally liquefied through heating.
  • Asphalt pavements can also be produced using bitumen that has been blended with solvents (known as cutbacks) or bitumen that has been dispersed in water (known as asphalt emulsions).
  • Asphalt pavements can include reclaimed or recycled materials containing reclaimed asphalt pavements (RAP), reclaimed asphalt shingles (RAS), ground tire rubber, and other post-consumer waste materials. Asphalt pavement deteriorates over time from oxidation of asphalt binder, heavy loads, moisture damage and varying climatic conditions resulting in fatigue cracking which then further accelerates the deterioration of the overall pavement.
  • Methods for restoring or repairing deteriorated asphalt pavement include removing and replacing the existing pavement with either newly prepared or recycled pavement.
  • the lifetime of existing pavement may also be extended by applying certain surface treatments.
  • the disclosed sterol-containing asphalt binder can retard, reduce or otherwise overcome the effects of aging in asphalt so as to preserve or retain some or all of the original properties of the virgin binder or virgin asphalt originally used when laying down the asphalt.
  • a surface treatment comprising sterol-containing asphalt binder, wherein sterol is added to an asphalt binder from 0.5 to 15 wt. % of the sterol based on the asphalt binder;
  • FIG. 1 A depicts an asphalt pavement structure.
  • FIG. 1 B depicts the asphalt pavement structure of FIG. 1 A with a surface treatment.
  • FIG. 1 C depicts the asphalt pavement with an interlayer.
  • FIG. 2 graphically depicts m-critical compared to days of oven aging at 75° C.
  • FIG. 3 graphically depicts S-critical compared to days of oven aging at 75° C.
  • FIG. 4 graphically depicts ⁇ Tc compared to days of oven aging at 75° C.
  • FIG. 5 graphically depicts R-value compared to days of oven aging at 75° C.
  • FIG. 6 graphically depicts high temperature PG grade at 1.0 kPa compared to days of aging at 75° C.
  • FIG. 7 graphically depicts S-critical and m-critical properties of binder recovered from the top and second half inch of compacted specimens after 60 days of oven aging.
  • FIG. 8 graphically depicts ⁇ Tc and R-Value properties of binder recovered from the top and second half inch of compacted specimens after 60 days of oven aging.
  • FIG. 9 graphically depicts S-critical and m-critical properties of binder recovered from the top and second half inch of compacted specimens after 152 days of oven aging.
  • FIG. 10 graphically depicts ⁇ Tc and R-Value properties of binder recovered from the top and second half inch of compacted specimens after 152 days of oven aging.
  • sterols can retard, reduce or otherwise overcome some of the effects of asphalt aging so as to preserve or retain some or all of the original properties of virgin asphalt binder. See International Application Nos. PCT/US16/037077, PCT/US16/64950 and PCT/US16/064961, PCT/US17/045887 each of which is incorporated herein by reference in its entirety.
  • the sterol was particularly effective when the binders contained reclaimed or recycled materials such as RAP, RAS or combinations of both; or when the binder contained paraffinic additives such as paraffinic base oils or re-refined engine oil bottoms (REOB) which are often used to soften binders.
  • reclaimed or recycled materials such as RAP, RAS or combinations of both
  • binder contained paraffinic additives such as paraffinic base oils or re-refined engine oil bottoms (REOB) which are often used to soften binders.
  • paraffinic additives such as paraffinic base oils or re-refined engine oil bottoms (REOB) which are often used to soften binders.
  • “Aged” refers to hard, poor-quality, or out-of-specification virgin asphalt or virgin binder, particularly virgin binders having a ring-and-ball softening point greater than 65° C. by EN 1427 and a penetration value at 25° C. by EN 1426 less than or equal to 12 dmm.
  • Aggregate and “construction aggregate” refer to particulate mineral material such as limestone, granite, trap rock, gravel, crushed gravel sand, crushed stone, crushed rock and slag useful in paving and pavement applications.
  • Adphalt refers to a binder and aggregate and optionally other components that are suitable for mixing with aggregate and binder. Depending on local usage, the terms “asphalt mix” or “mix” may be used interchangeably with the term “asphalt.”
  • Binder refers to a highly viscous liquid or semi-solid form of petroleum. “Binder” can include, for example bitumen. The term “asphalt binder” is used interchangeably with the term “binder.”
  • “Bitumen” refers to a class of black or dark-colored (solid, semisolid, or viscous) cementitious substances, natural or manufactured, composed principally of high molecular weight hydrocarbons, of which asphalts, tars, pitches, and asphaltenes are typical.
  • “Crude” when used with respect to a material containing a sterol means sterol that has not been fully refined and can contain components in addition to sterol.
  • m-critical or “Creep critical” grade refers to the low temperature relaxation grade of a binder.
  • the creep critical temperature is the temperature at which the slope of the flexural creep stiffness versus creep time according to ASTM (the Bending Beam Rheometer (BBR) test has an absolute value of 0.300.
  • the creep critical temperatures can also be determined from a 4 mm Dynamic Shear Rheometer (DSR) test at a value of ⁇ 0.275.
  • “Neat” or “Virgin” binders are binders not yet used in or recycled from asphalt pavement or asphalt shingles, and can include Performance Grade binders.
  • “Pure” when used with respect to a sterol or mixture of sterols means having at least a technical grade of purity or at least a reagent grade of purity.
  • Reclaimed asphalt and “recycled asphalt” refer to reclaimed asphalt pavement, reclaimed asphalt shingles, and reclaimed binder from old pavements, shingle manufacturing scrap, roofing felt, and other asphalt-containing products or applications.
  • Reclaimed asphalt pavement and “RAP” refer to asphalt that has been removed or excavated from a previously used road or pavement or other similar structure, and processed for reuse by any of a variety of well-known methods, including milling, ripping, breaking, crushing, or pulverizing.
  • Reclaimed asphalt shingles and “RAS” refer to shingles from sources including roof tear-off, manufacture's waste asphalt shingles and post-consumer waste.
  • S-Critical or “stiffness critical” grade refers to the low temperature stiffness grade of a binder.
  • the stiffness critical temperature is the temperature at which a binder tested according to ASTM D6648 has a flexural creep stiffness value of 300 MPa or as determined by either the Bending Beam Rheometer test or 4 mm DSR test as described in ⁇ Tc.
  • Softening agent refers to low viscosity additives that ease (or facilitate) the mixing and incorporation of a recycled binder into virgin binder during an asphalt production process.
  • Steprol additive refers to sterols or sterol mixes that can be combined with binder to retard the rate of aging of asphalt or binder, or to restore or renew aged asphalt or aged binder to provide some or all of the original properties of virgin asphalt or virgin binder.
  • Steprol blend refers to a composition, mixture or blend of pure sterols and crude sterols that can be combined with aged binder (e.g. recycled or reclaimed asphalt) to retard the rate of aging of asphalt binder, or to restore or renew the aged binder to provide some or all of the original properties of virgin asphalt or virgin binder.
  • aged binder e.g. recycled or reclaimed asphalt
  • ⁇ Tc refers to the value obtained when the low temperature creep or m-value critical temperature is subtracted from the low temperature stiffness critical temperature.
  • DSR dynamic shear rheometer
  • FIG. 1 is a cross-section of a portion of a typical asphalt pavement.
  • Crushed aggregate is applied as a base course atop a subgrade, which may be soil.
  • the crushed aggregate base course may for example have an average thickness of about 152 mm (6 inches) to about 305 mm (12 inches).
  • Atop the aggregate base course can be applied one or more asphalt layers.
  • FIG. 1 illustrates two asphalt layers, referred to as an asphalt pavement underlayer and an asphalt pavement topcoat.
  • the asphalt pavement underlayer may for example have an average thickness of about 57 mm (2.25 inches) to about 305 mm (12 inches) paved in several lifts, or 57 mm (2.25 inches) to about 127 mm (5 inches) paved in several lifts; and the asphalt pavement topcoat may for example have an average thickness of about 38 mm (1.5 inches) to about 102 mm (4 inches) or 38 mm (1.5 inches) to 63 mm (2.5 inches). It should be noted that the thickness is also dictated by the maximum aggregate size.
  • underlayer and topcoat that qualify the asphalt layers should be understood as relative terms. The further the asphalt layer is from the base course, the more “top” the asphalt layer is considered. The topmost asphalt layer—topcoat is exposed to weather and the elements such as sun, rain, snow, and freezing and thawing. The pavement also experiences frictional wear, fractures and other damage due to vehicular traffic. Over time, these environmental and service factors cause the asphalt pavement, particularly the surface layer, to deteriorate.
  • the entire pavement namely from the base course up to the topmost asphalt layer, with sterol-containing asphalt paving materials because over time the asphalt layers age.
  • Aging is not limited to the uppermost portion of the asphalt pavement (e.g., the uppermost 38 mm to 65 mm of compacted pavement).
  • the asphalt binder tends to age most severely at the surface, and the degree of aging and consequent detrimental impact on the binder typically decreases with pavement depth, and without regard to the materials that may have been added to the binder or other components of the paving material.
  • the topmost asphalt layer or layers can be paved with sterol-containing asphalt binder paving material. Doing so can retard binder aging throughout the asphalt pavement by making the topcoat layer more resistant to aging and meanwhile protecting the underlying asphalt pavement for an extended time period from weather, elements and other damage caused by premature deterioration of the topcoat layer. For example, by retarding asphalt aging, particularly in the topmost layer or layers, surface cracking that is associated with aged binders can be reduced thereby reducing air movement into the underlying pavement and the associated oxidation.
  • the replacement portion can be applied in many different configurations such that only the topmost 12 mm (0.5 inches) to 19 mm (0.75 inches) or the topmost 12 mm (0.5 inches) to 38 mm (1.5 inches) is applied as a thin overlay that contains a binder with sterol.
  • two 38 mm lifts may be applied with only the topmost 38 mm including a binder with sterol.
  • the milled out 76 mm (3 inches) or 102 mm (4 inches) can be replaced with two 50 mm (2 inch) lifts or a 50 mm (2 inch) lift with a 25 mm (1 inch) thin overlay (viz., a thinlay), with only the topmost lift or overlay including a binder with sterol.
  • compositions and methods for addressing pavement deterioration include preserving and maintaining an existing pavement with the aid of sterol-containing surface treatments disclosed herein.
  • sterols may be employed as an asphalt blend component in surface treatments for pavement preservation.
  • Asphalt surface treatment is a broad term embracing several asphalt types and asphalt-aggregate applications that may be used to extend the structural life of the underlying pavement. Such surface treatments usually are less than 25 millimeter (1 inch) thick and may be applied to any kind of road surface.
  • the road surface may for example be a primed granular base, or an existing asphalt or Portland cement concrete pavement. Surface treatments applied to an existing pavement surface are often called seal coats. Surface treatments commonly called chip seals are applied by spraying an asphalt emulsion and immediately spreading and rolling onto the applied emulsion an aggregate cover.
  • a sandwich seal is another surface treatment technique, in which a large aggregate is placed first, an asphalt emulsion (normally polymer modified) is sprayed onto the aggregate, and immediately followed by an application of smaller aggregate on top of the emulsion to lock in the seal.
  • a Cape seal is a single surface treatment followed by a slurry seal or micro-surfacing layer to fill in the voids. These and other surface treatments may be applied multiple times as desired.
  • the sterol-containing asphalt binder can be applied as a tack coat and as a fog seal.
  • bitumen used in the surface treatment can contain polymer additives derived from classes such as styrene butadiene rubber (SBR) lattices, styrene butadiene styrene (SBS) block copolymers, reactive ethylene terpolymers (RET), ground tire rubber, acrylic lattices, neoprene lattices, ethylene vinyl acetate (EVA) and polybutene.
  • SBR styrene butadiene rubber
  • SBS styrene butadiene styrene
  • RET reactive ethylene terpolymers
  • EVA ethylene vinyl acetate
  • any polymer that can be incorporated into asphalt in hot, cutback or emulsified form is a candidate.
  • Some surface treatments are based solely on asphalt emulsions as the binder (for example slurry seals and micro-surfacing). Chip seals can be constructed using an emulsion, hot applied asphalt binder, or cutback asphalt. The choice of binder type to use for chip seals is often dictated by the region or climate. The addition of sterol to any of these treatments can favorably impact binder aging in the surface treatment, thus prolonging the useful life of the surface treatment which in turn provides extended protection against aging for pavement beneath the surface treatment.
  • the primary ingredients include sterol additive added to a binder.
  • the disclosed sterol additives preferably can alter (e.g., reduce or retard) an asphalt binder aging rate, or can restore or renew an aged or recycled binder to provide some or all of the properties of a virgin asphalt binder.
  • the disclosed compositions and methods use a class of plant-derived chemistry, the sterol class of compounds. While plant sterols do not contain the same number of condensed or partially unsaturated rings as asphaltenes, they do have the benefit of not being a linear or branched linear molecule. For example, a sterol can alter or improve physical and rheological characteristics such as stiffness, effective temperature range, and low temperature properties of an asphalt binder.
  • the sterol additive belongs to the class of triterpenoids, and in particular to sterols or stanols.
  • the disclosed sterols e.g. triterpenoids
  • asphaltenes include extensive condensed ring systems with some level of unsaturation.
  • the asphaltene content of typical binders can range from less than 10% to more than 20%.
  • Asphaltenes are typically described as materials that are insoluble in n-heptane. An exact structure is unknown and based on the performance behavior of different binders it is unlikely that the asphaltene structure in any two binders is the same, especially those from different crude sources.
  • Asphaltenes give a binder its color and stiffness and they increase in content as the binder ages.
  • asphaltene content increases.
  • asphaltene content along with other products of oxidation such as carbonyls and sulfoxides are responsible for the stiffening of bituminous mixtures and their ultimate failure.
  • asphaltenes are not readily soluble in aliphatic chemicals.
  • Aromatic solvents will readily dissolve asphaltenes and aromatic process oils have been used in recycled mixtures. However, these oils may contain polynuclear aromatic compounds including listed potential carcinogens and therefore are not desirable additives.
  • Most plant based oils are straight or branched chain hydrocarbons with some level of unsaturation and therefore are not as effective at retarding aging as they are at softening the overall binders in a mixture.
  • Triterpenoids are a major group of plant natural products that include sterols, triterpene saponins, and related structures. Triterpenoids can be natural or synthetic. Typically, they are obtained by extraction from plant material. Extraction processes for the isolation of triterpenoids are described e.g. in international application publication numbers WO 2001/72315 A1 and WO 2004/016336 A1, the disclosures of which are each incorporated herein by reference in their entirety.
  • the triterpenoids include plant sterols and plant stanols.
  • the disclosed triterpenoids include the esterified and non-esterified forms of any of the plant sterols mentioned herein.
  • Exemplary pure plant sterols include campesterol, stigasterol, stigmasterol, ⁇ -sitosterol, ⁇ 5-avenosterol, ⁇ 7-stigasterol, ⁇ 7-avenosterol, brassicasterol or mixtures thereof.
  • the sterol blend contains ⁇ -sitosterol as the pure sterol.
  • the sterol blend contains a mixture of pure sterols.
  • Commercially available pure sterols and mixtures of pure sterols include those available from MP Biomedicals (Catalog No.
  • beta-Sitosterol (beta-Sitosterol ⁇ 40-60%; campesterol ⁇ 20-40%; Stigmasterol ⁇ 5%).
  • the pure sterol can include pure cholesterol. Cholesterol is shown here to have similar effects as plant sterols.
  • a pure sterol can have at least 70 wt. % sterols, and in some embodiments can have at least 80 wt %, at least 85 wt % or at least 95 wt % sterols.
  • Exemplary crude plant sterols include modified or unmodified natural products containing significant quantities of sterols, including such diverse plant sources as corn oil, wheat germ oil, sarsaparilla root, soybean pitch and corn oil pitch.
  • tall oil pitch can be obtained indirectly from the process of preparing paper from wood, particularly pine wood.
  • tall oil is a product of wood pulping (for example by the Kraft process), of which tall oil pitch is a by-product of the distillation of tall oil.
  • Tall oil pitch is an extremely complex material that can contain rosins, fatty acids, oxidation products and esterified materials, an appreciable fraction of which are sterol esters. Plant sources of crude sterols are inexpensive in that they are the foots or tailings left from various manufacturing processes.
  • the crude sterol sources include stigmasterol, ⁇ -sitosterol, campesterol, ergosterol, brassicasterol, cholesterol and lanosterol or mixtures thereof.
  • the crude sterol sources include soybean oil, corn oil, rice bran oil, peanut oil, sunflower seed oil, safflower oil, cottonseed oil, rapeseed oil, coffee seed oil, wheat germ oil, tall oil, and wool grease.
  • the crude sterol includes a bio-derived source or partially distilled residue of the bio-derived source.
  • the crude sterol source includes tall oil pitch, soybean oil or corn oil.
  • any of the oil tailings or pitches from the disclosed plant sources are suitable crude sterol sources.
  • U.S. Pat. No. 2,715,638, Aug. 16, 1955, to Albrecht, discloses a process for recovering sterols from tall oil pitch whereby the fatty acid impurities are removed by a neutralization process. Following this, the sterol esters are saponified; the free sterols are then recovered and washed with isopropanol and dried.
  • the crude sterols preferably are obtained from plant sources.
  • the crude sterol can include components in addition to the desired sterol or sterols.
  • Exemplary plant sources for crude sterols include tall oil pitch, crude tall oil, sugar cane oil, hot well skimmings, cottonseed pitch, soybean pitch, corn oil pitch, wheat germ oil or rye germ oil.
  • tall oil pitch is a source of the crude sterol.
  • Tall oil pitch can include about 30 to 40% unsaponifiable molecules. Unsaponifiables are molecules that do not react with alkali hydroxides. Fatty and rosin acids remaining in the tall oil pitch readily react with potassium or sodium hydroxides and thus the unsaponifiables can be readily separated.
  • a tall oil pitch sample can contain approximately 13.5% to 18% sterol molecules by weight.
  • the crude sterol can have less than a food grade of purity (e.g., less than 85 wt. % sterols) or contain more than 85 wt. % sterols but also can contain impurities or contaminants that render the material unsuitable for use in foods.
  • the crude sterol may be animal derived. In some embodiments, the crude sterol is cholesterol.
  • the disclosed sterol can be used in any combination that includes animal derived, plant derived, pure or crude.
  • the sterol is pure sterol from plants.
  • the sterol is pure sterol that is a combination of plant derived and animal derived.
  • the sterol is crude sterol from a combination of plant derived and animal derived.
  • the sterol added to the asphalt binder may for example range from about 0.5 to about 15 wt. %, from about 1 to about 10 wt. %, or from about 1 to about 3 wt. % of the binder in an asphalt. In some embodiments, the sterol added to the asphalt binder may for example range from about 0.5 to about 15 wt. %, from about 1 to about 10 wt. %, or from about 1 to about 3 wt. % of a virgin binder in an asphalt.
  • the sterol is a sterol blend in which the pure sterol:crude sterol blend added to an asphalt binder may for example range from about 0.5 to about 15 wt. %, or about 1 to about 10 wt. %, about 1 to about 3 wt. % of the virgin binder in an asphalt composition.
  • the sterol blends in some embodiments include a 10:90 to 90:10 ratio of pure sterol to crude sterol.
  • the sterol blends in some embodiments include at least a 20:80, 30:70 or 40:60 ratio of pure sterol to crude sterol, and in some embodiments include less than an 80:20, 70:30 or 60:40 ratio of pure sterol to crude sterol.
  • sterol can alter, reduce or retard the degradation of rheological properties due to aging in binders containing recycled bituminous materials such as RAS and/or RAP combined with softening agents such as, REOB, virgin paraffin or naphthenic base oils, untreated or non-rerefined waste drain oils or waste engine oil materials, vacuum tower asphalt extenders, paraffinic or naphthenic processing oils or lubricating base oils.
  • softening agents such as, REOB, virgin paraffin or naphthenic base oils, untreated or non-rerefined waste drain oils or waste engine oil materials, vacuum tower asphalt extenders, paraffinic or naphthenic processing oils or lubricating base oils.
  • sterol can alter, reduce or retard the degradation of rheological properties due to aging in binders containing recycled bituminous materials such as RAS and/or RAP combined with softening agents such as bio-derived oils or additives.
  • bio-dereived oils or additives include oils or esters from natural or biological resources, including derivatives or modifications thereof.
  • bio-derived oils or additives include one or more of a vegetable oil or ester thereof, a seed oil or ester thereof, a soybean oil or ester thereof, a corn oil or ester thereof, a cashew oil or ester thereof, a palm oil or ester thereof, a canola oil or ester thereof, a safflower oil or ester thereof, a sunflower oil or ester thereof, a citrus oil or ester thereof, pine oil or ester thereof, a rosin oil or ester thereof, or a bio-derived fatty acid ester.
  • Exemplary commercially available bio-derived oils or additives include those available from Cargill Incorporated under the Agri-Pure GoldTM brand (such as Agri-Pure Gold 53, 55, 63S, 67, 135, 142S, 200, 500, 750S, and 2000) and the AnovaTM brand asphalt bio-derived agents.
  • the sterol can alter, reduce or retard the degradation of rheological properties due to aging in binders containing recycled bituminous materials such as RAP, RAS, combinations of both RAP and RAS, or softening agents with RAP, RAS, or combinations of both RAP and RAS.
  • the binders used can include any binder known in the art and from any region, naturally occurring or manufactured.
  • Asphalt-based binders include petroleum-based binders.
  • Suitable asphalt-based or asphalt binders include those binders complying with ASTM D-6373, D-3387, D-946, AASHTO M320, M332, M226, or M20.
  • Some asphalt paving can include recycled materials such as RAP and RAS as components in the asphalt being paved.
  • RAP concentrations can be as high as 50% and RAS concentrations can be as high as 6% by weight of the paving mixture.
  • the typical binder content of RAP is in the range of 4-6% by weight and the typical binder content of RAS is in the range of 20-25% by weight. Consequently, a mixture containing 50% by weight of RAP will contain 2.5% to 3% RAP binder contributed to the final binder mixture and a binder mixture containing 6% RAS by weight will contain 1.2% to 1.5% RAS binder contributed to the final binder mixture.
  • the disclosed binders containing sterol can provide recycled asphalt (e.g. RAP or RAS) having improved physical and rheological characteristics such as reduced stiffness, more effective temperature range, and desirable low temperature properties.
  • recycled asphalt e.g. RAP or RAS
  • the asphalt may contain other components in addition to the disclosed sterol-containing asphalt binder.
  • Such other components can include elastomers, non-bituminous binders, adhesion promoters, softening agents, rejuvenating agents and other suitable components.
  • Useful elastomers include, for example, ethylene-vinyl acetate copolymers, polybutadienes, ethylene-propylene copolymers, ethylene-propylene-diene terpolymers, reactive ethylene terpolymers (e.g. ELVALOYTM), butadiene-styrene block copolymers, styrene-butadiene-styrene (SBS) block copolymers, isoprene-styrene block copolymers and styrene-isoprene-styrene (SIS) block copolymers, chloroprene polymers (e.g., neoprenes) and the like.
  • ELVALOYTM reactive ethylene terpolymers
  • SBS styrene-butadiene-styrene
  • SIS styrene-isoprene-styrene
  • Cured elastomer additives may include ground tire rubber materials. For example, see the 2015 Standard Specifications for the State of California (Section 37, pg. 423), and Section 39 for Hot Mix Asphalt, starting on pg. 447 and available at http://www.dot.ca.gov/dist1/d1lab/SECTION %2039%20%20HMA.pdf and http://caltrans-opac.ca.gov/publicat.htm.
  • the asphalt binder may be prepared by mixing or blending sterol with binder (e.g. virgin binder) to form a mixture or blend.
  • binder e.g. virgin binder
  • the mixture or blend can be added to recycled asphalt materials (e.g. RAS and/or RAP) and aggregate.
  • RAS and/or RAP recycled asphalt materials
  • a method of preparing an asphalt mix involves mixing or blending a sterol with virgin asphalt at a temperature from about 100° C. to about 250° C. or from about 130° C. to about 200° C.
  • the sterol is mixed with the virgin asphalt at a temperature from about 125° C. to about 175° C., or 180° C. to 205° C.
  • the virgin asphalt is combined with sterol and softening agent.
  • the virgin binder is combined and mixed with sterol and aggregate to form an asphalt pavement material.
  • the virgin binder is combined and mixed with binder extracted from RAP, RAS or a combination of RAP and RAS, sterol and aggregate to form an asphalt pavement material.
  • the mixture of asphalt and aggregate is then applied by a paving machine to a surface which is usually roller compacted by additional equipment while still at an elevated temperature. The compacted aggregate and asphalt binder eventually stiffens upon cooling to form a pavement.
  • the disclosed sterol-containing asphalt binder can be applied to the topmost asphalt layers of a road pavement by to other process such as cold-mix process where the aggregate, cold and moist, is mixed with a hot or cold binder, which can be an emulsion of asphalt dispersed in water using a suitable surfactant or a mixture of asphalt and a suitable hydrocarbon solvent, such as naphtha, #1 oil, or #2 oil, to name a few (generally referred to as a cutback asphalt).
  • a suitable surfactant or a mixture of asphalt and a suitable hydrocarbon solvent such as naphtha, #1 oil, or #2 oil, to name a few (generally referred to as a cutback asphalt).
  • a suitable surfactant or a mixture of asphalt and a suitable hydrocarbon solvent such as naphtha, #1 oil, or #2 oil, to name a few (generally referred to as a cutback asphalt).
  • a suitable hydrocarbon solvent such as naphtha, #1 oil, or #2 oil, to name a
  • the binder can also be foamed and mixed with the aggregate to enhance the coating efficacy.
  • Some emulsions also utilize hydrocarbon solvents in addition to water to produce materials suitable for specific applications.
  • Warm mix processes may also be used to form a pavement in which the topmost asphalt layer of the pavement includes a sterol-containing asphalt binder.
  • a method of making a road pavement such that, a sterol-containing asphalt binder is provided wherein a sterol is added to a virgin asphalt binder from 0.5 to 15 wt. % of the sterol based on the virgin asphalt binder; combining the asphalt binder containing sterol with aggregate to form an asphalt paving material; applying the asphalt paving material atop an asphalt pavement layer; and compacting the applied asphalt paving material to form a road pavement.
  • the asphalt paving material can be compacted to form a road pavement to a suitable density, typically 89% or greater of maximum theoretical density depending on aggregate gradation and position within the pavement layer to form a road pavement.
  • a method for treating an asphalt-containing surface comprising providing a surface treatment comprising sterol-containing asphalt binder, wherein sterol is added to an asphalt binder from 0.5 to 15 wt. % of the sterol based on the asphalt binder; and applying the surface treatment to the surface of an existing pavement.
  • the binder includes a blend of binders.
  • the binder blend includes virgin binder and binder extracted from reclaimed asphalt.
  • the binder extracted from RAS material may be extracted from manufacturer asphalt shingle waste, from consumer asphalt shingle waste, or from a mixture of binders extracted from manufacturer and consumer asphalt shingle waste.
  • a binder blend may include from about 60 wt % to about 95 wt % of virgin binder and sterol from about 0.5 wt % to about 15.0 wt % of the virgin asphalt.
  • a binder blend may further include 5 wt % to about 40 wt % of binder extracted from reclaimed asphalt such as RAP, or RAS or a combination of RAP and RAS.
  • the sterol additive has been shown in to improve high and low temperature properties and PG grading for both low and high temperature ends of RAP- or RAS-containing asphalt binder blends.
  • the asphalt pavement material can be applied as the topmost layer of a road pavement, with the topmost layer having an average thickness of for example up to about 38 mm or up to about 65 mm. In some embodiments, the asphalt pavement material is applied as the topmost layer of the road pavement, with the topmost layer having an average thickness of for example up to about 12 mm or up to about 38 mm.
  • ⁇ Tc Delta Tc
  • ⁇ 5° C. is more negative than ⁇ 3° C. and therefore a ⁇ Tc value of ⁇ 5° C. is worse than a ⁇ Tc value of ⁇ 3° C.
  • the ⁇ Tc parameter can also be determined using a Bending Beam Rheometer (BBR) test procedure based on AASHTO T313 or ASTM D6648. It is important that when the BBR test procedure is used that the test is conducted at a sufficient number of temperatures such that results for the Stiffness failure criteria of 300 MPa and Creep or m-value failure criteria of 0.300 are obtained with one result being below the failure criteria and one result being above the failure criteria. In some instances for binders with ⁇ Tc values less than ⁇ 5° C. this can require performing the BBR test at three or more test temperatures. ⁇ Tc values calculated from data when the BBR criteria requirements referred to above are not met may not be accurate.
  • BBR Bending Beam Rheometer
  • the sterol-containing asphalt binder can provide an asphalt binder composition with a ⁇ Tc of greater than or equal to ⁇ 5.0° C. In some embodiments, the sterol-containing asphalt binder can provide an asphalt binder with a ⁇ Tc of greater than or equal to ⁇ 5.0° C. after 27, 60, 90 and 152 hours of aging at 75° C. In still other embodiments, the sterol-containing asphalt binder can provide an asphalt binder with a less negative ⁇ Tc value and a decreased R-Value following aging, when compared to a similarly-aged asphalt binder without the sterol.
  • the sterol-containing asphalt binder can provide an asphalt binder composition, a pavement, or surface treatment it is added on a ⁇ Tc of ⁇ 5.0° C. to +5° C., from ⁇ 4° C. to +4° C. or from ⁇ 3° C. to +5° C.
  • emulsions are typically used to apply asphalt surface treatments.
  • Typical emulsions include aqueous emulsions with the asphalt binder particles dispersed in water containing one or more emulsifying agents.
  • the emulsifying agents used in the emulsion can include any known cationic, anionic, nonionic, or amphoteric surfactants.
  • asphalt emulsions are classified in ASTM D977 and D2397 by the time it takes for “set” or “cure”: rapid setting (RS), medium setting (MS) or slow setting (SS).
  • Emulsions cure through evaporation of the water.
  • Some emulsions (e.g., cationic emulsions) also cure through electrochemical deposition of the dispersed asphalt particles on the surface of the aggregate. This is a process of coalescence as the asphalt particles migrate to the aggregate surface and then the asphalt particles join together or coalesce to form a uniform asphalt layer.
  • Emulsifying agents can also be classified based on their surface charge (or lack thereof) as cationic, anionic, nonionic, or amphoteric. By combining the surface charge characteristic with the setting time, emulsifiers used for paving applications can be classified as, for example, cationic rapid setting (CRS), cationic medium setting (CMS), and cationic slow setting (CSS). These classifications are known in the art and can be readily measured as set forth in ASTM D977 and D2397.
  • the asphalt emulsions can contain other agents such as polymers, solvents and other additives as described herein.
  • the disclosed surface treatments are aqueous emulsions that include sterol-containing asphalt binder.
  • the binder may be formed by mixing a sterol into an asphalt binder (e.g. virgin binder). The binder containing sterol is then dispersed in a continuous water phase with the help of an emulsifying agent.
  • the emulsifying agent and preheated asphalt are typically pumped into a colloid mill where high shear mixing produces an asphalt emulsion having asphalt droplets dispersed in the water.
  • the asphalt emulsions are polymer modified, e.g., to increase the strength and durability of the resulting asphalt-based, cold paving formulations and to decrease the curing times of these formulations.
  • Suitable polymer lattices for microsurfacing surface layer formulations include cationic SBR (styrene-butadiene rubber) lattices, natural rubber lattices, and polychloroprene lattices (e.g., NEOPRENETM lattices available from Denka Performance Elastomer LLC).
  • SBR styrene-butadiene rubber
  • natural rubber lattices natural rubber lattices
  • polychloroprene lattices e.g., NEOPRENETM lattices available from Denka Performance Elastomer LLC.
  • SBS poly(styrene-butadiene-styrene) block copolymers and copolymers such as ethylene, ethylene vinyl acetate (EVA), glycidyl methacrylate terpolymers or ethylene, n-butyl acrylate (nBA), glycidyl methacrylate terpolymers can also be used but typically must be added slowly to heated asphalt (e.g. 160-170° C.), and then subjected to high shear mixing to disperse the polymer in the asphalt prior to forming the asphalt emulsion.
  • EVA ethylene vinyl acetate
  • nBA n-butyl acrylate
  • glycidyl methacrylate terpolymers can also be used but typically must be added slowly to heated asphalt (e.g. 160-170° C.), and then subjected to high shear mixing to disperse the polymer in the asphalt prior to forming the asphalt emulsion.
  • Commercial terpolymers
  • the sterol-containing emulsion preferably includes between about 0.1 wt % and about 10 wt surfactants, 55 wt % to 95 wt % of a sterol-containing asphalt binder with water making up the total.
  • the surface to be treated Prior to application of the emulsion, the surface to be treated is usually cleaned to remove excess surface dirt, weeds, and contaminants by, for example, brushing the surface, blasting the surface with compressed air, or washing the surface.
  • the emulsion can be applied using any suitable method for applying a liquid to a porous surface, such as brushing, wiping and drawing, or spraying.
  • Spraying is a preferred emulsion application method because a thin emulsion layer can be applied in a short time period.
  • the emulsion is preferably applied at a temperature between 10 (15° F.) to 93° C. (200° F.) or between 15° C. (60° F.) and 87° C. (190° F.).
  • the emulsion desirably has a viscosity at the application temperature that allows it to be sprayed upon the surface and preferably has a viscosity of from 1 to 5 centipoise.
  • the disclosed sterol-containing asphalt binder can also be used in any cold-in-place recycling (CIR) process known in the art.
  • CIR involves the removal, reprocessing and relaying of part of an existing asphalt surface without the use of heat.
  • CIR processes can be economical because they reduce costs from, for example, reusing existing material, minimizing use of new materials, decreasing material transportation and hauling demands and not heating the material.
  • CIR can include the removal of the top inches of an existing asphalt pavement.
  • CIR can be used, among other things, to create a new pavement layer using the old pavement, remove cracks, ruts and potholes and rehabilitate a pavement surface. In some embodiments, the top 1 inch or more to the top 6 inches or less can be removed. Removal for CIR is generally performed by milling or grinding. Milling desirably is performed using a milling machine or using machines referred as reclaimers.
  • CIR as the name implies is performed on the grade in a continuous process.
  • the removed material is generally passed through a crusher which is component part of the CIR paving train prior to being mixed with emulsion or foamed asphalt.
  • the removed material can then be crushed and/or graded to produce a desired gradation.
  • a desired gradation can specify a maximum particle size only.
  • One example of a gradation is the removed material is less than 11 ⁇ 4 inch nominal size. Another example is the removed material is less than 1 inch in nominal size. Virgin aggregate can be added to the removed material.
  • the material can then be mixed with an asphalt emulsion having a sterol-containing asphalt binder, lime, Portland cement or fly ash.
  • the mixing can be performed by any machine known in the art including, but not limited to, a milling machine or a pug mill.
  • the material can then be returned to the milled surface and graded. Examples of machines that can be used for these steps are asphalt pavers and motor graders.
  • sterol-containing asphalt binder is diluted or “cut” with solvents as part of a complex composition or network, which may further include functional additives such as polymers and surfactants as well as inert additives such as filler clays and cellulose fibers. These additives are included in cutback formulations to provide compositions with specific functional properties such as viscosity, elasticity adhesion and cure rate.
  • Cutbacks are used because their viscosity is lower than that of neat asphalt and can thus be used in low temperature applications. After a cutback is applied, the solvent evaporates at different rates depending on the volatility of the solvent used to produce the cutback. As the solvent evaporates the viscosity of the remaining asphalt binder increases resulting in an increasingly stable mixture with aggregate. A cutback asphalt is said to “cure” as the petroleum solvent evaporates away.
  • Exemplary cutback solvents include petroleum solvents, Light Cycle Oil (LCO) and #2 Diesel Fuel. naphtha, #1 oil, or #2 oil, to name a few.
  • LCO Light Cycle Oil
  • Diesel Fuel naphtha, #1 oil, or #2 oil, to name a few.
  • cutback asphalts are defined by American Society of Testing and Materials (ASTM) specifications as follows:
  • SC Slow cure type (Road Oils): ASTM D-2026-72
  • MC Medium cure type: ASTM D-2027-76
  • the cutback may for example contain from 50 to 96 wt % asphalt binder, 70 to 90 wt % asphalt binder, or 75 to 85% asphalt binder, with the remainder being cutback solvent.
  • the cutback asphalt may contain conventional amounts of antistrip or other additives.
  • the disclosed sterol-containing asphalt binder can also be used an interlayer.
  • FIG. 1 C illustrates interlayers as layers that maybe placed between an old asphalt pavement and a newly applied asphalt layer. Interlayers are typically an asphalt mix with a high binder amount.
  • an interlayer mix contains 6% to 12% polymer modified binder and 88% to 94% crushed aggregate.
  • the binder is produced by modifying a blend of virgin binder and 0.5% to 15% sterol with an elastomer. Examples of materials requirements can be found at the Iowa DOT specification SS-15006, “Supplemental Specifications for Hot Mix Asphalt Interlayer.”
  • the asphalt binder (polymer modified or not) contains the disclosed sterol.
  • bituminous mixtures were Wisconsin specification 3 million Equivalent Single Axel Load (ESAL) mixture containing Reclaimed Asphalt Pavement (RAP) yielding a 0.2 binder replacement ratio using (4.5% by weight) virgin PG 58S-28 asphalt binder for a total binder content of 5.6%.
  • ESAL Equivalent Single Axel Load
  • RAP Reclaimed Asphalt Pavement
  • These bituminous mixtures were compacted to a target air voids level of 6% to 8% using two gyratory compactors referenced by the prefix T and P.
  • the gyratory compactors referenced T were manufactured by Troxler Electronic Laboratories, Inc. of Research Triangle Park, N.C.
  • the gyratory compactors referenced P were manufactured by Pine Instrument Company of Grove City, Pa.
  • Group III of twenty specimens was treated with the equivalent of 0.2 gallons/yd 2 of a cationic quick set (CQS) emulsion produced from a PG 64S-22 to which 5% phytosterol had been added prior to emulsification.
  • the percent residue of the CQS emulsion was in each case between 65% and 66%.
  • a foam brush was used to apply the emulsion by weight to the tops of the gyratory specimens that had been inserted into the sewer pipe.
  • the tops of the gyratory specimens were the tops of the compacted specimens as removed from the gyratory molds.
  • the air voids of all specimens were determined using AASHTO T-166 and recorded for the unique alpha numerical identifier assigned to each specimen.
  • the outside of the sewer pipe containing each specimen was labeled as “untreated”, “CQS”, or “CQS+sterol” as well as being labeled with a T or P followed by the unique numerical identifier assigned to that particular specimen.
  • the three groups of twenty specimens per group were further separated into three groups of ten specimens.
  • Each sub group of ten specimens contained 10 untreated specimens, 10 CQS treated specimens and 10 CQS+sterol treated specimens and each group of 10 specimens contained five T and five P specimens.
  • One subgroup of thirty specimens was placed in a forced draft oven held at 75° C. for aging and the other subgroup of thirty specimens was placed out in the open to be aged naturally. The oven conditioned samples were removed from the oven after 27, 60, 90, and 152 days of conditioning at 75° C.
  • Tables 1 through 5 summarize the data obtained by testing binder samples recovered from top 1 ⁇ 2 inch layer of the compacted mixture specimens for the untreated, CQS emulsion, and CQS emulsion produced from asphalt containing 5% of plant sterols.
  • Table 1 is the base or control data for all the treatments. Table 1 data was recovered from a compacted mix specimen, which received no treatment and had not been aged.
  • Tables 2 through 5 summarize the recovered binder data after 27, 60, 90, and 152 days of aging at 75° C. in a forced draft oven.
  • Both the PG Grade at 1.0 kPa and 2.2 kPa provide an indication of the relative change in binder stiffness. The higher the temperature at which the binder achieves a stiffness of 1.0 kPa or 2.2 kPa the more aged that binder has become.
  • the low temperature Stiffness Critical temperature (S-critical) and the relaxation critical temperature (m-critical) track the change in the low temperature grade of the recovered binder.
  • the parameter labeled ⁇ Tc is determined by subtracting the m-critical value from the S-critical value. The more negative the ⁇ Tc result becomes the more susceptible to fatigue cracking the mixture containing that binder becomes. Values of ⁇ Tc less than ⁇ 5° C. for a binder are indicative of mixture susceptible to fatigue cracking.
  • the R-value parameter is an indication of the ability of a binder to relax stress. Binders with higher R-values have more trouble relaxing stress and consequently are more prone to cracking.
  • FIGS. 2 to 6 show the data from Tables 1 through 5 plotted for easier interpretation.
  • the low temperature m-critical value ( FIG. 2 ) is the low temperature PG grade of the binder.
  • the m-critical temperature is obtained from the slope measured at 60 seconds of the relaxation modulus master curve.
  • the m-critical slope value can be obtained from the Bending Beam Rheometer or test (ASTM D6648) or from the 4 mm DSR test as shown by the research of Sui and Farrar at Western Research Institute.
  • the sterol addition showed improving the ability of the binder to relax stresses at low and intermediate temperatures.
  • FIG. 3 is a plot of the low temperature S-critical or Stiffness Critical value at the different aging times.
  • FIG. 3 shows that there is minor variation in the S-critical values between treatments at any given aging time. It is also worth emphasizing that although the S-critical temperatures are colder than the m-critical temperatures the PG binder specifications for the low temperature failing grade of the binder is based on the warmer of these two low temperature values. Therefore, if an additive can slow down the rate at which the m-critical value degrades then the binder will have better low temperature performance.
  • FIG. 4 is a plot of the ⁇ Tc value at the different aging times.
  • FIG. 4 shows that initially (at 27 days) the addition of both the CQS and CQS+sterol emulsions to the mix specimens improved the ⁇ Tc values for those two treatments relative to the original ⁇ Tc at zero time.
  • the recovered binder for the untreated samples shows that ⁇ Tc decreased by more than 2° C., whereas ⁇ Tc for the plain CQS treated samples decreased only about 0.5° C.
  • the ⁇ Tc value for the CQS+sterol treated samples increased by 0.6° C.
  • the additional asphalt binder added to the original specimens accounted for a reduced rate of aging for the CQS treated specimens and the additional asphalt binder plus the impact of the sterol accounted for the improvement of the recovered binder after 27 days of aging relative to the ⁇ Tc of zero-day aged mix.
  • the ⁇ Tc values of binder recovered from the CQS+sterol treated specimens were still greater than ⁇ 5° compared to ⁇ Tc for the untreated and CQS treated specimens.
  • Even after 152 days of aging the CQS+sterol treated specimens have a better ⁇ Tc value compared to the other treatments.
  • FIG. 5 is a plot of the binder Rheological index or R-Value for the different treatments.
  • the R-value is another indicator of the ability of a binder to relax stress. Binders with increasing R-Values have decreased ability to relax stress. It is desirable to keep R-Value under 3 and as FIG. 5 shows the initial application of the emulsion treatments reduced the R-values for those two treatments, but by 60 hours of aging the untreated and CQS treated specimens had values greater than 3. Through the entire aging sequence, the CQS+sterol treated specimens had consistently better R-values than the other treatments.
  • FIG. 6 is a plot of the high temperature PG grade of binders recovered from the various treatments with aging time. The data shows relatively minor variation in high temperature grade with aging; however, the CQS+sterol treatment does consistently have the lowest high temperature value.
  • the high temperature property of the binder is not highly significant as long as the binder is stiff enough to resist rutting and for a typical upper Midwestern US climate, all of these binders possess sufficient stiffness.
  • Tables 6 and 7 show the properties of binders recovered from the 2nd 1 ⁇ 2 inch of the compacted specimens after 60 and 152 days of aging. The purpose of obtaining this data at these intervals was to show the aging of the binder in these layers compared to aging of the binder in the top 1 ⁇ 2 inch mixture layers. With the exception of the ⁇ Tc value for the 2nd 1 ⁇ 2 inch binder from the untreated specimen the properties of these recovered binders at 60 days and at 152 days are similar. The 60 day untreated sample with a ⁇ Tc of ⁇ 3.80° C. may be due to the warmer S-critical value for the untreated sample compared to the CQS and CQS+sterol treatments.
  • a warmer S-critical value indicates a greater aging of the stiffness failure temperature compared to the treated samples and could be due to more oxygen migration into the 2nd 1 ⁇ 2 inch of the mix. Because the untreated samples did not have any emulsion treatment, the surface half inch of those untreated specimens would have a greater opportunity for oxygen to permeate the mix.
  • the R-value for the untreated 60 day recovered binder is similar to the other two treatments which is consistent with similar properties of relaxation and also consistent with the similarities of the m-critical properties of all three treatments for the 2nd 1 ⁇ 2 inch recovered binders.
  • FIG. 7 shows bar chart comparisons of the S-critical and m-critical data between the top 1 ⁇ 2 inch and second 1 ⁇ 2 inch recovered binder at 60 days of aging.
  • FIG. 8 shows comparison between the ⁇ Tc and R-Value properties for the same binders at 60 days of aging.
  • FIGS. 9 and 10 show similar respective plots for the binders recovered from the top and second 1 ⁇ 2 inch of binders recovered after 152 days of aging.
  • the S-critical values show hardly any variation with respect to depth for any treatment and the m-critical value for the top 1 ⁇ 2 inch of the CQS+sterol treatment exhibits a 2.4° C. better low temperature m-critical value than the binder from the 2nd half inch.
  • the fact that the CQS treated specimens exhibited an m-critical value 0.6° C. better than the second half inch recovered binder shows that the additional binder added to the mix was not the source of the more greatly improved m-critical value in the CQS+sterol specimens and shows that the fog seal application of the emulsion containing the sterol resides in the top half inch layer.
  • the data plotted in FIG. 8 shows ⁇ Tc values for the top half inch and second half inch binders after 60 days.
  • the R-value for the top half inch of the sterol treated mix was also lower than the second half inch.
  • FIG. 9 shows S-critical and m-critical comparisons after 152 days of aging.
  • the S-critical data is very similar for all treatments for both layers.
  • the m-critical values show definite differences.
  • the second half inch layers were very similar with the untreated specimens having a slightly warmer m-critical temperature.
  • the CQS treated specimens had a m-critical value 2.67° C. cooler (i.e. better) for the top half inch compared to the second half inch ( ⁇ 10.09° C. vs. ⁇ 7.42° C.). This is attributable to the extra asphalt added in the fog seal.
  • the top half inch of the CQS+sterol however had an m-critical value that was 2.7° C. cooler (i.e.
  • FIG. 10 compares the ⁇ Tc and R-values for the three treatments after 152 days of conditioning.
  • the ⁇ Tc values for both layers of the untreated specimens and the second half-inch of the CQS and CQS+sterol treatments are all similar with the emulsion treated specimens being slightly better, most likely due to the asphalt added to the surface of those specimens.
  • the CQS treated specimens had a top half-inch layer ⁇ Tc 2.2° C. better than the second half-inch binder, but the CQS+sterol top half inch layer ⁇ Tc was 5° C. better than the second half inch layer.
  • the R-value data also shows similar relative performance.
  • the untreated specimens have nearly identical R-values
  • the CQS treated specimens show that the top half inch binder has a 0.25 R-value improvement over the second half inch binder and the CQS+sterol treated specimens have a top half inch binder has a 0.74 R-value improvement over the binder in the second half inch.

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Abstract

Pavement aging can be reduced by applying to an asphalt-containing pavement a topcoat layer or a surface treatment containing asphalt binder with sterols.

Description

BACKGROUND
Asphalt pavement is a composite material that is a mixture of mineral aggregate and a liquefied asphalt (bitumen) binder, which hardens to form a robust surface. The bitumen is generally liquefied through heating. Asphalt pavements can also be produced using bitumen that has been blended with solvents (known as cutbacks) or bitumen that has been dispersed in water (known as asphalt emulsions). Asphalt pavements can include reclaimed or recycled materials containing reclaimed asphalt pavements (RAP), reclaimed asphalt shingles (RAS), ground tire rubber, and other post-consumer waste materials. Asphalt pavement deteriorates over time from oxidation of asphalt binder, heavy loads, moisture damage and varying climatic conditions resulting in fatigue cracking which then further accelerates the deterioration of the overall pavement.
Methods for restoring or repairing deteriorated asphalt pavement include removing and replacing the existing pavement with either newly prepared or recycled pavement. The lifetime of existing pavement may also be extended by applying certain surface treatments.
SUMMARY
Disclosed is a method of using sterol in asphalt compositions and methods that may be used for constructing a topmost portion of the pavement and surface treatments for pavement preservation and maintenance. The disclosed sterol-containing asphalt binder can retard, reduce or otherwise overcome the effects of aging in asphalt so as to preserve or retain some or all of the original properties of the virgin binder or virgin asphalt originally used when laying down the asphalt.
In one embodiment is a method of road paving comprising:
    • providing sterol-containing asphalt binder, wherein sterol is added to an asphalt binder from 0.5 to 15 wt. % of the sterol based on the asphalt binder;
    • combining the sterol-containing asphalt binder with aggregate to form an asphalt paving material;
    • applying the asphalt paving material atop an asphalt pavement layer; and
    • compacting the applied asphalt paving material to form a road pavement having a sterol-containing topcoat layer.
In another embodiment is disclosed a method for treating an asphalt-containing surface comprising:
providing a surface treatment comprising sterol-containing asphalt binder, wherein sterol is added to an asphalt binder from 0.5 to 15 wt. % of the sterol based on the asphalt binder; and
applying the surface treatment to the surface of an existing pavement.
BRIEF DESCRIPTION OF DRAWINGS
FIG. 1A depicts an asphalt pavement structure.
FIG. 1B depicts the asphalt pavement structure of FIG. 1A with a surface treatment.
FIG. 1C depicts the asphalt pavement with an interlayer.
FIG. 2 graphically depicts m-critical compared to days of oven aging at 75° C.
FIG. 3 graphically depicts S-critical compared to days of oven aging at 75° C.
FIG. 4 graphically depicts ΔTc compared to days of oven aging at 75° C.
FIG. 5 graphically depicts R-value compared to days of oven aging at 75° C.
FIG. 6 graphically depicts high temperature PG grade at 1.0 kPa compared to days of aging at 75° C.
FIG. 7 graphically depicts S-critical and m-critical properties of binder recovered from the top and second half inch of compacted specimens after 60 days of oven aging.
FIG. 8 graphically depicts ΔTc and R-Value properties of binder recovered from the top and second half inch of compacted specimens after 60 days of oven aging.
FIG. 9 graphically depicts S-critical and m-critical properties of binder recovered from the top and second half inch of compacted specimens after 152 days of oven aging.
FIG. 10 graphically depicts ΔTc and R-Value properties of binder recovered from the top and second half inch of compacted specimens after 152 days of oven aging.
DETAILED DESCRIPTION
Disclosed is the use of sterols in compositions and methods that may be used for pavement construction or pavement preservation and maintenance. Applicants have previously shown that sterols can retard, reduce or otherwise overcome some of the effects of asphalt aging so as to preserve or retain some or all of the original properties of virgin asphalt binder. See International Application Nos. PCT/US16/037077, PCT/US16/64950 and PCT/US16/064961, PCT/US17/045887 each of which is incorporated herein by reference in its entirety. The sterol was particularly effective when the binders contained reclaimed or recycled materials such as RAP, RAS or combinations of both; or when the binder contained paraffinic additives such as paraffinic base oils or re-refined engine oil bottoms (REOB) which are often used to soften binders.
Headings are provided herein solely for ease of reading and should not be interpreted as limiting.
Abbreviations, Acronyms & Definitions
“Aged” refers to hard, poor-quality, or out-of-specification virgin asphalt or virgin binder, particularly virgin binders having a ring-and-ball softening point greater than 65° C. by EN 1427 and a penetration value at 25° C. by EN 1426 less than or equal to 12 dmm.
“Aggregate” and “construction aggregate” refer to particulate mineral material such as limestone, granite, trap rock, gravel, crushed gravel sand, crushed stone, crushed rock and slag useful in paving and pavement applications.
“Asphalt” refers to a binder and aggregate and optionally other components that are suitable for mixing with aggregate and binder. Depending on local usage, the terms “asphalt mix” or “mix” may be used interchangeably with the term “asphalt.”
“Binder” refers to a highly viscous liquid or semi-solid form of petroleum. “Binder” can include, for example bitumen. The term “asphalt binder” is used interchangeably with the term “binder.”
“Bitumen” refers to a class of black or dark-colored (solid, semisolid, or viscous) cementitious substances, natural or manufactured, composed principally of high molecular weight hydrocarbons, of which asphalts, tars, pitches, and asphaltenes are typical.
“Crude” when used with respect to a material containing a sterol means sterol that has not been fully refined and can contain components in addition to sterol.
“m-critical” or “Creep critical” grade refers to the low temperature relaxation grade of a binder. The creep critical temperature is the temperature at which the slope of the flexural creep stiffness versus creep time according to ASTM (the Bending Beam Rheometer (BBR) test has an absolute value of 0.300. The creep critical temperatures can also be determined from a 4 mm Dynamic Shear Rheometer (DSR) test at a value of −0.275.
“Neat” or “Virgin” binders are binders not yet used in or recycled from asphalt pavement or asphalt shingles, and can include Performance Grade binders.
“Pure” when used with respect to a sterol or mixture of sterols means having at least a technical grade of purity or at least a reagent grade of purity.
“Reclaimed asphalt” and “recycled asphalt” refer to reclaimed asphalt pavement, reclaimed asphalt shingles, and reclaimed binder from old pavements, shingle manufacturing scrap, roofing felt, and other asphalt-containing products or applications.
“Reclaimed asphalt pavement” and “RAP” refer to asphalt that has been removed or excavated from a previously used road or pavement or other similar structure, and processed for reuse by any of a variety of well-known methods, including milling, ripping, breaking, crushing, or pulverizing.
“Reclaimed asphalt shingles” and “RAS” refer to shingles from sources including roof tear-off, manufacture's waste asphalt shingles and post-consumer waste.
“S-Critical” or “stiffness critical” grade refers to the low temperature stiffness grade of a binder. The stiffness critical temperature is the temperature at which a binder tested according to ASTM D6648 has a flexural creep stiffness value of 300 MPa or as determined by either the Bending Beam Rheometer test or 4 mm DSR test as described in ΔTc.
“Softening agent” refers to low viscosity additives that ease (or facilitate) the mixing and incorporation of a recycled binder into virgin binder during an asphalt production process.
“Sterol additive” refers to sterols or sterol mixes that can be combined with binder to retard the rate of aging of asphalt or binder, or to restore or renew aged asphalt or aged binder to provide some or all of the original properties of virgin asphalt or virgin binder.
“Sterol blend” refers to a composition, mixture or blend of pure sterols and crude sterols that can be combined with aged binder (e.g. recycled or reclaimed asphalt) to retard the rate of aging of asphalt binder, or to restore or renew the aged binder to provide some or all of the original properties of virgin asphalt or virgin binder.
“ΔTc” refers to the value obtained when the low temperature creep or m-value critical temperature is subtracted from the low temperature stiffness critical temperature. The 4 mm dynamic shear rheometer (DSR) test and analysis procedures are described by Sui, C., Farrar, M., Tuminello, W., Turner, T., A New Technique for Measuring low-temperature Properties of Asphalt Binders with Small Amounts of Material, Transportation Research Record: No 1681, TRB 2010. See also Sui, C., Farrar, M. J., Harnsberger, P. M., Tuminello, W. H., Turner, T. F., New Low Temperature Performance Grading Method Using 4 mm Parallel Plates on a Dynamic Shear Rheometer. TRB Preprint CD, 2011, and by Farrar, M., et al., (2012), Thin Film Oxidative Aging and Low Temperature Performance Grading Using Small Plate Dynamic Shear Rheometry: An Alternative to Standard RTFO, PAV and BBr. Eurasphalt & Eurobitume 5th E&E Congress-2012 Istanbul (pp. Paper O5ee-467). Istanbul: Foundation Euraspalt.
All weights, parts and percentages are based on weight unless otherwise specified.
FIG. 1 is a cross-section of a portion of a typical asphalt pavement. Crushed aggregate is applied as a base course atop a subgrade, which may be soil. The crushed aggregate base course may for example have an average thickness of about 152 mm (6 inches) to about 305 mm (12 inches). Atop the aggregate base course can be applied one or more asphalt layers. FIG. 1 illustrates two asphalt layers, referred to as an asphalt pavement underlayer and an asphalt pavement topcoat. The asphalt pavement underlayer may for example have an average thickness of about 57 mm (2.25 inches) to about 305 mm (12 inches) paved in several lifts, or 57 mm (2.25 inches) to about 127 mm (5 inches) paved in several lifts; and the asphalt pavement topcoat may for example have an average thickness of about 38 mm (1.5 inches) to about 102 mm (4 inches) or 38 mm (1.5 inches) to 63 mm (2.5 inches). It should be noted that the thickness is also dictated by the maximum aggregate size.
The terms “underlayer” and “topcoat” that qualify the asphalt layers should be understood as relative terms. The further the asphalt layer is from the base course, the more “top” the asphalt layer is considered. The topmost asphalt layer—topcoat is exposed to weather and the elements such as sun, rain, snow, and freezing and thawing. The pavement also experiences frictional wear, fractures and other damage due to vehicular traffic. Over time, these environmental and service factors cause the asphalt pavement, particularly the surface layer, to deteriorate.
Ideally, one would construct the entire pavement, namely from the base course up to the topmost asphalt layer, with sterol-containing asphalt paving materials because over time the asphalt layers age. Aging is not limited to the uppermost portion of the asphalt pavement (e.g., the uppermost 38 mm to 65 mm of compacted pavement). However, the asphalt binder tends to age most severely at the surface, and the degree of aging and consequent detrimental impact on the binder typically decreases with pavement depth, and without regard to the materials that may have been added to the binder or other components of the paving material.
Although a sterol may be added to an entire asphalt pavement, sterols are somewhat expensive. To control costs, however, the topmost asphalt layer or layers can be paved with sterol-containing asphalt binder paving material. Doing so can retard binder aging throughout the asphalt pavement by making the topcoat layer more resistant to aging and meanwhile protecting the underlying asphalt pavement for an extended time period from weather, elements and other damage caused by premature deterioration of the topcoat layer. For example, by retarding asphalt aging, particularly in the topmost layer or layers, surface cracking that is associated with aged binders can be reduced thereby reducing air movement into the underlying pavement and the associated oxidation. Similarly, by retarding asphalt aging in the topmost layer or layers, moisture uptake in the topcoat layer and moisture transmission through that layer or through cracks in that layer can be reduced, thereby limiting further damage to the pavement and increases in its aging rate. By lengthening the time at which the binder reaches a condition where pavement distress begins the overall pavement life is improved.
When a pavement is to be resurfaced, one might mill away, for example the upper 76 mm (3 inches) to 102 mm (4 inches) of old pavement and replace part or all of the milled portion with a sterol-containing replacement portion. The replacement portion can be applied in many different configurations such that only the topmost 12 mm (0.5 inches) to 19 mm (0.75 inches) or the topmost 12 mm (0.5 inches) to 38 mm (1.5 inches) is applied as a thin overlay that contains a binder with sterol. For example, two 38 mm lifts may be applied with only the topmost 38 mm including a binder with sterol. As another example, the milled out 76 mm (3 inches) or 102 mm (4 inches) can be replaced with two 50 mm (2 inch) lifts or a 50 mm (2 inch) lift with a 25 mm (1 inch) thin overlay (viz., a thinlay), with only the topmost lift or overlay including a binder with sterol.
Other compositions and methods for addressing pavement deterioration include preserving and maintaining an existing pavement with the aid of sterol-containing surface treatments disclosed herein. In such treatments, sterols may be employed as an asphalt blend component in surface treatments for pavement preservation.
Asphalt surface treatment is a broad term embracing several asphalt types and asphalt-aggregate applications that may be used to extend the structural life of the underlying pavement. Such surface treatments usually are less than 25 millimeter (1 inch) thick and may be applied to any kind of road surface. The road surface may for example be a primed granular base, or an existing asphalt or Portland cement concrete pavement. Surface treatments applied to an existing pavement surface are often called seal coats. Surface treatments commonly called chip seals are applied by spraying an asphalt emulsion and immediately spreading and rolling onto the applied emulsion an aggregate cover. A sandwich seal is another surface treatment technique, in which a large aggregate is placed first, an asphalt emulsion (normally polymer modified) is sprayed onto the aggregate, and immediately followed by an application of smaller aggregate on top of the emulsion to lock in the seal. A Cape seal is a single surface treatment followed by a slurry seal or micro-surfacing layer to fill in the voids. These and other surface treatments may be applied multiple times as desired. In some embodiments, the sterol-containing asphalt binder can be applied as a tack coat and as a fog seal.
Taking into consideration factors such as the region and climate, surface treatments that include sterol-containing asphalt binder may be applied as an emulsion, hot applied bitumen or cutback. In all cases, the bitumen used in the surface treatment can contain polymer additives derived from classes such as styrene butadiene rubber (SBR) lattices, styrene butadiene styrene (SBS) block copolymers, reactive ethylene terpolymers (RET), ground tire rubber, acrylic lattices, neoprene lattices, ethylene vinyl acetate (EVA) and polybutene. This list should not be taken as limiting because any polymer that can be incorporated into asphalt in hot, cutback or emulsified form is a candidate. Some surface treatments are based solely on asphalt emulsions as the binder (for example slurry seals and micro-surfacing). Chip seals can be constructed using an emulsion, hot applied asphalt binder, or cutback asphalt. The choice of binder type to use for chip seals is often dictated by the region or climate. The addition of sterol to any of these treatments can favorably impact binder aging in the surface treatment, thus prolonging the useful life of the surface treatment which in turn provides extended protection against aging for pavement beneath the surface treatment.
Whatever pavement construction process is used, the primary ingredients include sterol additive added to a binder.
Sterol Additive
The disclosed sterol additives preferably can alter (e.g., reduce or retard) an asphalt binder aging rate, or can restore or renew an aged or recycled binder to provide some or all of the properties of a virgin asphalt binder. The disclosed compositions and methods use a class of plant-derived chemistry, the sterol class of compounds. While plant sterols do not contain the same number of condensed or partially unsaturated rings as asphaltenes, they do have the benefit of not being a linear or branched linear molecule. For example, a sterol can alter or improve physical and rheological characteristics such as stiffness, effective temperature range, and low temperature properties of an asphalt binder.
In some embodiments, the sterol additive belongs to the class of triterpenoids, and in particular to sterols or stanols. The disclosed sterols (e.g. triterpenoids) can effectively work with asphaltenes. Asphaltenes include extensive condensed ring systems with some level of unsaturation. The asphaltene content of typical binders can range from less than 10% to more than 20%. Asphaltenes are typically described as materials that are insoluble in n-heptane. An exact structure is unknown and based on the performance behavior of different binders it is unlikely that the asphaltene structure in any two binders is the same, especially those from different crude sources. Asphaltenes give a binder its color and stiffness and they increase in content as the binder ages. Consequently, the addition of RAP and/or RAS causes the asphaltene content to increase. Increasing asphaltene content along with other products of oxidation such as carbonyls and sulfoxides are responsible for the stiffening of bituminous mixtures and their ultimate failure. By their very chemical nature asphaltenes are not readily soluble in aliphatic chemicals. Aromatic solvents will readily dissolve asphaltenes and aromatic process oils have been used in recycled mixtures. However, these oils may contain polynuclear aromatic compounds including listed potential carcinogens and therefore are not desirable additives. Most plant based oils are straight or branched chain hydrocarbons with some level of unsaturation and therefore are not as effective at retarding aging as they are at softening the overall binders in a mixture.
Triterpenoids are a major group of plant natural products that include sterols, triterpene saponins, and related structures. Triterpenoids can be natural or synthetic. Typically, they are obtained by extraction from plant material. Extraction processes for the isolation of triterpenoids are described e.g. in international application publication numbers WO 2001/72315 A1 and WO 2004/016336 A1, the disclosures of which are each incorporated herein by reference in their entirety.
The triterpenoids include plant sterols and plant stanols. The disclosed triterpenoids include the esterified and non-esterified forms of any of the plant sterols mentioned herein.
Exemplary pure plant sterols include campesterol, stigasterol, stigmasterol, β-sitosterol, Δ5-avenosterol, Δ7-stigasterol, Δ7-avenosterol, brassicasterol or mixtures thereof. In some embodiments, the sterol blend contains β-sitosterol as the pure sterol. In other embodiments, the sterol blend contains a mixture of pure sterols. Commercially available pure sterols and mixtures of pure sterols include those available from MP Biomedicals (Catalog No. 02102886) referred to as beta-Sitosterol (beta-Sitosterol ˜40-60%; campesterol ˜20-40%; Stigmasterol ˜5%). In some embodiments, the pure sterol can include pure cholesterol. Cholesterol is shown here to have similar effects as plant sterols.
In some embodiments, a pure sterol can have at least 70 wt. % sterols, and in some embodiments can have at least 80 wt %, at least 85 wt % or at least 95 wt % sterols.
Exemplary crude plant sterols include modified or unmodified natural products containing significant quantities of sterols, including such diverse plant sources as corn oil, wheat germ oil, sarsaparilla root, soybean pitch and corn oil pitch. For example, tall oil pitch can be obtained indirectly from the process of preparing paper from wood, particularly pine wood. For example, tall oil is a product of wood pulping (for example by the Kraft process), of which tall oil pitch is a by-product of the distillation of tall oil. Tall oil pitch is an extremely complex material that can contain rosins, fatty acids, oxidation products and esterified materials, an appreciable fraction of which are sterol esters. Plant sources of crude sterols are inexpensive in that they are the foots or tailings left from various manufacturing processes.
In some embodiments, the crude sterol sources include stigmasterol, β-sitosterol, campesterol, ergosterol, brassicasterol, cholesterol and lanosterol or mixtures thereof. In some embodiments, the crude sterol sources include soybean oil, corn oil, rice bran oil, peanut oil, sunflower seed oil, safflower oil, cottonseed oil, rapeseed oil, coffee seed oil, wheat germ oil, tall oil, and wool grease. In some embodiments, the crude sterol includes a bio-derived source or partially distilled residue of the bio-derived source. In some embodiments, the crude sterol source includes tall oil pitch, soybean oil or corn oil.
Any of the oil tailings or pitches from the disclosed plant sources are suitable crude sterol sources. U.S. Pat. No. 2,715,638, Aug. 16, 1955, to Albrecht, discloses a process for recovering sterols from tall oil pitch whereby the fatty acid impurities are removed by a neutralization process. Following this, the sterol esters are saponified; the free sterols are then recovered and washed with isopropanol and dried.
The crude sterols preferably are obtained from plant sources. The crude sterol can include components in addition to the desired sterol or sterols. Exemplary plant sources for crude sterols include tall oil pitch, crude tall oil, sugar cane oil, hot well skimmings, cottonseed pitch, soybean pitch, corn oil pitch, wheat germ oil or rye germ oil. In some embodiments, tall oil pitch is a source of the crude sterol. Tall oil pitch can include about 30 to 40% unsaponifiable molecules. Unsaponifiables are molecules that do not react with alkali hydroxides. Fatty and rosin acids remaining in the tall oil pitch readily react with potassium or sodium hydroxides and thus the unsaponifiables can be readily separated. It has been shown that 45% of the unsaponifiable fraction can include sitosterols. Therefore, a tall oil pitch sample can contain approximately 13.5% to 18% sterol molecules by weight. In some embodiments the crude sterol can have less than a food grade of purity (e.g., less than 85 wt. % sterols) or contain more than 85 wt. % sterols but also can contain impurities or contaminants that render the material unsuitable for use in foods.
In some embodiments, the crude sterol may be animal derived. In some embodiments, the crude sterol is cholesterol.
It should be understood that the disclosed sterol can be used in any combination that includes animal derived, plant derived, pure or crude. For example, in some embodiments the sterol is pure sterol from plants. In some embodiments, the sterol is pure sterol that is a combination of plant derived and animal derived. In some embodiments, the sterol is crude sterol from a combination of plant derived and animal derived.
The sterol added to the asphalt binder may for example range from about 0.5 to about 15 wt. %, from about 1 to about 10 wt. %, or from about 1 to about 3 wt. % of the binder in an asphalt. In some embodiments, the sterol added to the asphalt binder may for example range from about 0.5 to about 15 wt. %, from about 1 to about 10 wt. %, or from about 1 to about 3 wt. % of a virgin binder in an asphalt.
In some embodiments, the sterol is a sterol blend in which the pure sterol:crude sterol blend added to an asphalt binder may for example range from about 0.5 to about 15 wt. %, or about 1 to about 10 wt. %, about 1 to about 3 wt. % of the virgin binder in an asphalt composition. The sterol blends, in some embodiments include a 10:90 to 90:10 ratio of pure sterol to crude sterol. The sterol blends in some embodiments include at least a 20:80, 30:70 or 40:60 ratio of pure sterol to crude sterol, and in some embodiments include less than an 80:20, 70:30 or 60:40 ratio of pure sterol to crude sterol.
In some embodiments, sterol can alter, reduce or retard the degradation of rheological properties due to aging in binders containing recycled bituminous materials such as RAS and/or RAP combined with softening agents such as, REOB, virgin paraffin or naphthenic base oils, untreated or non-rerefined waste drain oils or waste engine oil materials, vacuum tower asphalt extenders, paraffinic or naphthenic processing oils or lubricating base oils.
In some embodiments, sterol can alter, reduce or retard the degradation of rheological properties due to aging in binders containing recycled bituminous materials such as RAS and/or RAP combined with softening agents such as bio-derived oils or additives. Such bio-dereived oils or additives include oils or esters from natural or biological resources, including derivatives or modifications thereof. Non-limiting examples of bio-derived oils or additives include one or more of a vegetable oil or ester thereof, a seed oil or ester thereof, a soybean oil or ester thereof, a corn oil or ester thereof, a cashew oil or ester thereof, a palm oil or ester thereof, a canola oil or ester thereof, a safflower oil or ester thereof, a sunflower oil or ester thereof, a citrus oil or ester thereof, pine oil or ester thereof, a rosin oil or ester thereof, or a bio-derived fatty acid ester. Exemplary commercially available bio-derived oils or additives include those available from Cargill Incorporated under the Agri-Pure Gold™ brand (such as Agri-Pure Gold 53, 55, 63S, 67, 135, 142S, 200, 500, 750S, and 2000) and the Anova™ brand asphalt bio-derived agents.
In embodiments, the sterol can alter, reduce or retard the degradation of rheological properties due to aging in binders containing recycled bituminous materials such as RAP, RAS, combinations of both RAP and RAS, or softening agents with RAP, RAS, or combinations of both RAP and RAS.
Binders
The binders used can include any binder known in the art and from any region, naturally occurring or manufactured. Asphalt-based binders include petroleum-based binders. Suitable asphalt-based or asphalt binders include those binders complying with ASTM D-6373, D-3387, D-946, AASHTO M320, M332, M226, or M20.
Some asphalt paving can include recycled materials such as RAP and RAS as components in the asphalt being paved. Typically, RAP concentrations can be as high as 50% and RAS concentrations can be as high as 6% by weight of the paving mixture. The typical binder content of RAP is in the range of 4-6% by weight and the typical binder content of RAS is in the range of 20-25% by weight. Consequently, a mixture containing 50% by weight of RAP will contain 2.5% to 3% RAP binder contributed to the final binder mixture and a binder mixture containing 6% RAS by weight will contain 1.2% to 1.5% RAS binder contributed to the final binder mixture.
The disclosed binders containing sterol can provide recycled asphalt (e.g. RAP or RAS) having improved physical and rheological characteristics such as reduced stiffness, more effective temperature range, and desirable low temperature properties.
Other Additives
The asphalt may contain other components in addition to the disclosed sterol-containing asphalt binder. Such other components can include elastomers, non-bituminous binders, adhesion promoters, softening agents, rejuvenating agents and other suitable components.
Useful elastomers include, for example, ethylene-vinyl acetate copolymers, polybutadienes, ethylene-propylene copolymers, ethylene-propylene-diene terpolymers, reactive ethylene terpolymers (e.g. ELVALOY™), butadiene-styrene block copolymers, styrene-butadiene-styrene (SBS) block copolymers, isoprene-styrene block copolymers and styrene-isoprene-styrene (SIS) block copolymers, chloroprene polymers (e.g., neoprenes) and the like. Cured elastomer additives may include ground tire rubber materials. For example, see the 2015 Standard Specifications for the State of California (Section 37, pg. 423), and Section 39 for Hot Mix Asphalt, starting on pg. 447 and available at http://www.dot.ca.gov/dist1/d1lab/SECTION %2039%20%20HMA.pdf and http://caltrans-opac.ca.gov/publicat.htm.
The asphalt binder may be prepared by mixing or blending sterol with binder (e.g. virgin binder) to form a mixture or blend. In some embodiments, the mixture or blend can be added to recycled asphalt materials (e.g. RAS and/or RAP) and aggregate. One of skill in the art will recognize that any sequences of adding and mixing components are possible. In some embodiments, a method of preparing an asphalt mix involves mixing or blending a sterol with virgin asphalt at a temperature from about 100° C. to about 250° C. or from about 130° C. to about 200° C. In some embodiments, the sterol is mixed with the virgin asphalt at a temperature from about 125° C. to about 175° C., or 180° C. to 205° C. In some embodiments, the virgin asphalt is combined with sterol and softening agent. In still other embodiments, the virgin binder is combined and mixed with sterol and aggregate to form an asphalt pavement material. In other embodiments, the virgin binder is combined and mixed with binder extracted from RAP, RAS or a combination of RAP and RAS, sterol and aggregate to form an asphalt pavement material.
A mixture of a suitable aggregate comprising stones, gravel, sand, and the like, is heated at an elevated temperature of about 132-187° C. and mixed with a similarly hot, asphalt binder containing sterol until the aggregate particles are coated with the binder. Paving mixes made in this temperature range are often referred to as a hot mix. The mixture of asphalt and aggregate is then applied by a paving machine to a surface which is usually roller compacted by additional equipment while still at an elevated temperature. The compacted aggregate and asphalt binder eventually stiffens upon cooling to form a pavement.
The disclosed sterol-containing asphalt binder can be applied to the topmost asphalt layers of a road pavement by to other process such as cold-mix process where the aggregate, cold and moist, is mixed with a hot or cold binder, which can be an emulsion of asphalt dispersed in water using a suitable surfactant or a mixture of asphalt and a suitable hydrocarbon solvent, such as naphtha, #1 oil, or #2 oil, to name a few (generally referred to as a cutback asphalt). The emulsified asphalt particles coat and bind with the aggregate and remain after the water has evaporated. When a cutback asphalt is used, the hydrocarbon solvent evaporates at different rates depending on the volatility of the solvent. Regardless of the solvent volatility, what remains behind is a paving material where the asphalt component gradually hardens or stiffens over time as the solvent is removed (e.g. by evaporation).
The binder can also be foamed and mixed with the aggregate to enhance the coating efficacy. Some emulsions also utilize hydrocarbon solvents in addition to water to produce materials suitable for specific applications. Warm mix processes may also be used to form a pavement in which the topmost asphalt layer of the pavement includes a sterol-containing asphalt binder.
In one embodiment a method of making a road pavement is disclosed such that, a sterol-containing asphalt binder is provided wherein a sterol is added to a virgin asphalt binder from 0.5 to 15 wt. % of the sterol based on the virgin asphalt binder; combining the asphalt binder containing sterol with aggregate to form an asphalt paving material; applying the asphalt paving material atop an asphalt pavement layer; and compacting the applied asphalt paving material to form a road pavement. In some embodiments, the asphalt paving material can be compacted to form a road pavement to a suitable density, typically 89% or greater of maximum theoretical density depending on aggregate gradation and position within the pavement layer to form a road pavement.
In another embodiment, a method for treating an asphalt-containing surface comprising providing a surface treatment comprising sterol-containing asphalt binder, wherein sterol is added to an asphalt binder from 0.5 to 15 wt. % of the sterol based on the asphalt binder; and applying the surface treatment to the surface of an existing pavement.
In some embodiments, the binder includes a blend of binders. In some embodiments, the binder blend includes virgin binder and binder extracted from reclaimed asphalt. For example, the binder extracted from RAS material may be extracted from manufacturer asphalt shingle waste, from consumer asphalt shingle waste, or from a mixture of binders extracted from manufacturer and consumer asphalt shingle waste. In some embodiments, a binder blend may include from about 60 wt % to about 95 wt % of virgin binder and sterol from about 0.5 wt % to about 15.0 wt % of the virgin asphalt. In some embodiments, a binder blend may further include 5 wt % to about 40 wt % of binder extracted from reclaimed asphalt such as RAP, or RAS or a combination of RAP and RAS. The sterol additive has been shown in to improve high and low temperature properties and PG grading for both low and high temperature ends of RAP- or RAS-containing asphalt binder blends.
The asphalt pavement material can be applied as the topmost layer of a road pavement, with the topmost layer having an average thickness of for example up to about 38 mm or up to about 65 mm. In some embodiments, the asphalt pavement material is applied as the topmost layer of the road pavement, with the topmost layer having an average thickness of for example up to about 12 mm or up to about 38 mm.
A measure of how effectively different binders respond to aging or how effectively different additives impact the response of binders to aging is the parameter Delta Tc (ΔTc). ΔTc is calculated by subtracting the m-critical temperature from the S-critical temperature. Anderson et al. in their 2011 paper showed that larger values of ΔTc were well correlated to fatigue cracking of asphalt pavements. Specifically, that research showed that when ΔTc was 5° C. or greater cracking was very likely. Anderson, et al. used the procedure of subtracting the S-critical temperature from the m-critical temperature and thus the more positive the value of ΔTc the greater the chance of fatigue cracking. Since 2011 the asphalt research community has reversed the calculation as stated above and now the more negative values of ΔTc indicate decreasing binder performance. More recently Reinke, et al. presented research at the 2016 EE Congress in Prague, Czech Republic showing that the more negative values of ΔTc strongly correlated to fatigue cracking on two research projects in Minnesota, USA. (Reinke, Hanz, Anderson, Impact of re-refined engine oil bottoms on binder properties and mix performance on two pavements in Minnesota, 6th Eurasphalt and Eurobitume Congress, Prague, Jun. 1-3, 2016, DOI: dx.doi.org/10.14211/EE.2016.284). Therefore, in the industry and as used in the application, a ΔTc warning limit value is −3° C. and a potential failure value is −5° C. In other words, −5° C. is more negative than −3° C. and therefore a ΔTc value of −5° C. is worse than a ΔTc value of −3° C.
To determine the ΔTc parameter, a 4 mm DSR test procedure and data analysis methodology from the Western Research Institute was employed as noted above. The DSR test procedure and methodology are also disclosed in International Application No. PCT/US16/37077 filed Jun. 10, 2016, in PCT/US2016/064950 filed Dec. 5, 2016 and PCT/US2016/064961 filed Dec. 5, 2016, each of which is incorporated herein by reference in its entirety.
The ΔTc parameter can also be determined using a Bending Beam Rheometer (BBR) test procedure based on AASHTO T313 or ASTM D6648. It is important that when the BBR test procedure is used that the test is conducted at a sufficient number of temperatures such that results for the Stiffness failure criteria of 300 MPa and Creep or m-value failure criteria of 0.300 are obtained with one result being below the failure criteria and one result being above the failure criteria. In some instances for binders with ΔTc values less than −5° C. this can require performing the BBR test at three or more test temperatures. ΔTc values calculated from data when the BBR criteria requirements referred to above are not met may not be accurate.
In embodiments, the sterol-containing asphalt binder can provide an asphalt binder composition with a ΔTc of greater than or equal to −5.0° C. In some embodiments, the sterol-containing asphalt binder can provide an asphalt binder with a ΔTc of greater than or equal to −5.0° C. after 27, 60, 90 and 152 hours of aging at 75° C. In still other embodiments, the sterol-containing asphalt binder can provide an asphalt binder with a less negative ΔTc value and a decreased R-Value following aging, when compared to a similarly-aged asphalt binder without the sterol. In embodiments, the sterol-containing asphalt binder can provide an asphalt binder composition, a pavement, or surface treatment it is added on a ΔTc of −5.0° C. to +5° C., from −4° C. to +4° C. or from −3° C. to +5° C.
Emulsions
While pavement construction can use asphalt in emulsions, emulsions are typically used to apply asphalt surface treatments. Typical emulsions include aqueous emulsions with the asphalt binder particles dispersed in water containing one or more emulsifying agents.
The emulsifying agents used in the emulsion can include any known cationic, anionic, nonionic, or amphoteric surfactants. In paving applications, asphalt emulsions are classified in ASTM D977 and D2397 by the time it takes for “set” or “cure”: rapid setting (RS), medium setting (MS) or slow setting (SS). Emulsions cure through evaporation of the water. Some emulsions (e.g., cationic emulsions) also cure through electrochemical deposition of the dispersed asphalt particles on the surface of the aggregate. This is a process of coalescence as the asphalt particles migrate to the aggregate surface and then the asphalt particles join together or coalesce to form a uniform asphalt layer. This can be considered a chemical “break”. In any event, before an emulsion can cure or set, the emulsion typically breaks via separation of water from the asphalt particles. The breaking time is determined by the emulsion stability, and the more stable the emulsion, the longer the breaking time. Emulsifying agents can also be classified based on their surface charge (or lack thereof) as cationic, anionic, nonionic, or amphoteric. By combining the surface charge characteristic with the setting time, emulsifiers used for paving applications can be classified as, for example, cationic rapid setting (CRS), cationic medium setting (CMS), and cationic slow setting (CSS). These classifications are known in the art and can be readily measured as set forth in ASTM D977 and D2397.
The asphalt emulsions can contain other agents such as polymers, solvents and other additives as described herein.
The disclosed surface treatments are aqueous emulsions that include sterol-containing asphalt binder. The binder may be formed by mixing a sterol into an asphalt binder (e.g. virgin binder). The binder containing sterol is then dispersed in a continuous water phase with the help of an emulsifying agent. The emulsifying agent and preheated asphalt are typically pumped into a colloid mill where high shear mixing produces an asphalt emulsion having asphalt droplets dispersed in the water.
In micro-surfacing formulations and optionally for slurry seal operations, the asphalt emulsions are polymer modified, e.g., to increase the strength and durability of the resulting asphalt-based, cold paving formulations and to decrease the curing times of these formulations.
Suitable polymer lattices for microsurfacing surface layer formulations include cationic SBR (styrene-butadiene rubber) lattices, natural rubber lattices, and polychloroprene lattices (e.g., NEOPRENE™ lattices available from Denka Performance Elastomer LLC). SBS (poly(styrene-butadiene-styrene)) block copolymers and copolymers such as ethylene, ethylene vinyl acetate (EVA), glycidyl methacrylate terpolymers or ethylene, n-butyl acrylate (nBA), glycidyl methacrylate terpolymers can also be used but typically must be added slowly to heated asphalt (e.g. 160-170° C.), and then subjected to high shear mixing to disperse the polymer in the asphalt prior to forming the asphalt emulsion. Commercial terpolymers that may be used include ELVALOY™ available from E. I. DuPont de Nemours.
The sterol-containing emulsion preferably includes between about 0.1 wt % and about 10 wt surfactants, 55 wt % to 95 wt % of a sterol-containing asphalt binder with water making up the total. Prior to application of the emulsion, the surface to be treated is usually cleaned to remove excess surface dirt, weeds, and contaminants by, for example, brushing the surface, blasting the surface with compressed air, or washing the surface.
The emulsion can be applied using any suitable method for applying a liquid to a porous surface, such as brushing, wiping and drawing, or spraying. Spraying is a preferred emulsion application method because a thin emulsion layer can be applied in a short time period. The emulsion is preferably applied at a temperature between 10 (15° F.) to 93° C. (200° F.) or between 15° C. (60° F.) and 87° C. (190° F.). The emulsion desirably has a viscosity at the application temperature that allows it to be sprayed upon the surface and preferably has a viscosity of from 1 to 5 centipoise.
Cold-in Place Recycling
The disclosed sterol-containing asphalt binder can also be used in any cold-in-place recycling (CIR) process known in the art. CIR involves the removal, reprocessing and relaying of part of an existing asphalt surface without the use of heat. CIR processes can be economical because they reduce costs from, for example, reusing existing material, minimizing use of new materials, decreasing material transportation and hauling demands and not heating the material. CIR can include the removal of the top inches of an existing asphalt pavement. CIR can be used, among other things, to create a new pavement layer using the old pavement, remove cracks, ruts and potholes and rehabilitate a pavement surface. In some embodiments, the top 1 inch or more to the top 6 inches or less can be removed. Removal for CIR is generally performed by milling or grinding. Milling desirably is performed using a milling machine or using machines referred as reclaimers.
CIR as the name implies is performed on the grade in a continuous process. The removed material is generally passed through a crusher which is component part of the CIR paving train prior to being mixed with emulsion or foamed asphalt. The removed material can then be crushed and/or graded to produce a desired gradation. A desired gradation can specify a maximum particle size only. One example of a gradation is the removed material is less than 1¼ inch nominal size. Another example is the removed material is less than 1 inch in nominal size. Virgin aggregate can be added to the removed material.
The material can then be mixed with an asphalt emulsion having a sterol-containing asphalt binder, lime, Portland cement or fly ash. The mixing can be performed by any machine known in the art including, but not limited to, a milling machine or a pug mill. The material can then be returned to the milled surface and graded. Examples of machines that can be used for these steps are asphalt pavers and motor graders.
Cut Backs
In some embodiments, sterol-containing asphalt binder is diluted or “cut” with solvents as part of a complex composition or network, which may further include functional additives such as polymers and surfactants as well as inert additives such as filler clays and cellulose fibers. These additives are included in cutback formulations to provide compositions with specific functional properties such as viscosity, elasticity adhesion and cure rate.
Cutbacks are used because their viscosity is lower than that of neat asphalt and can thus be used in low temperature applications. After a cutback is applied, the solvent evaporates at different rates depending on the volatility of the solvent used to produce the cutback. As the solvent evaporates the viscosity of the remaining asphalt binder increases resulting in an increasingly stable mixture with aggregate. A cutback asphalt is said to “cure” as the petroleum solvent evaporates away.
Exemplary cutback solvents include petroleum solvents, Light Cycle Oil (LCO) and #2 Diesel Fuel. naphtha, #1 oil, or #2 oil, to name a few.
The types of cutback asphalts are defined by American Society of Testing and Materials (ASTM) specifications as follows:
SC=Slow cure type (Road Oils): ASTM D-2026-72
MC=Medium cure type: ASTM D-2027-76
RC=Rapid cure type: ASTM D-2028-76
The cutback may for example contain from 50 to 96 wt % asphalt binder, 70 to 90 wt % asphalt binder, or 75 to 85% asphalt binder, with the remainder being cutback solvent. In addition, the cutback asphalt may contain conventional amounts of antistrip or other additives.
Interlayers
The disclosed sterol-containing asphalt binder can also be used an interlayer. FIG. 1C illustrates interlayers as layers that maybe placed between an old asphalt pavement and a newly applied asphalt layer. Interlayers are typically an asphalt mix with a high binder amount.
In one exemplary embodiment, an interlayer mix contains 6% to 12% polymer modified binder and 88% to 94% crushed aggregate. The binder is produced by modifying a blend of virgin binder and 0.5% to 15% sterol with an elastomer. Examples of materials requirements can be found at the Iowa DOT specification SS-15006, “Supplemental Specifications for Hot Mix Asphalt Interlayer.” In some embodiments, the asphalt binder (polymer modified or not) contains the disclosed sterol.
EXAMPLES
The following study showed that the presence of sterol in a base asphalt binder used to produce an emulsion retards the aging of the binder in the top ½ inch of mix in compacted specimens relative to the untreated and only compacted specimens.
Specimens of bituminous mixtures used were Wisconsin specification 3 million Equivalent Single Axel Load (ESAL) mixture containing Reclaimed Asphalt Pavement (RAP) yielding a 0.2 binder replacement ratio using (4.5% by weight) virgin PG 58S-28 asphalt binder for a total binder content of 5.6%. These bituminous mixtures were compacted to a target air voids level of 6% to 8% using two gyratory compactors referenced by the prefix T and P. The gyratory compactors referenced T were manufactured by Troxler Electronic Laboratories, Inc. of Research Triangle Park, N.C. The gyratory compactors referenced P were manufactured by Pine Instrument Company of Grove City, Pa.
All specimens were compacted to a height of 95 mm and a diameter of 150 mm. All specimens were inserted into sleeves of approximately 97 mm in height cut from 6 inch internal diameter sewer pipe with a nominal ⅛ inch wall thickness. The tops and bottoms of the specimens remained exposed. The compacted specimens were separated into three groups, each group having 20 specimens (10 T and 10 P). Group I of twenty specimens received no treatment and was oven aged or naturally aged. Group II of twenty specimens was treated with the equivalent of 0.2 gallons/yd2 of a cationic quick set (CQS) emulsion produced from a PG 64S-22 base binder. Group III of twenty specimens was treated with the equivalent of 0.2 gallons/yd2 of a cationic quick set (CQS) emulsion produced from a PG 64S-22 to which 5% phytosterol had been added prior to emulsification. The percent residue of the CQS emulsion was in each case between 65% and 66%. A foam brush was used to apply the emulsion by weight to the tops of the gyratory specimens that had been inserted into the sewer pipe. The tops of the gyratory specimens were the tops of the compacted specimens as removed from the gyratory molds. The air voids of all specimens were determined using AASHTO T-166 and recorded for the unique alpha numerical identifier assigned to each specimen. The outside of the sewer pipe containing each specimen was labeled as “untreated”, “CQS”, or “CQS+sterol” as well as being labeled with a T or P followed by the unique numerical identifier assigned to that particular specimen.
The three groups of twenty specimens per group were further separated into three groups of ten specimens. Each sub group of ten specimens contained 10 untreated specimens, 10 CQS treated specimens and 10 CQS+sterol treated specimens and each group of 10 specimens contained five T and five P specimens. One subgroup of thirty specimens was placed in a forced draft oven held at 75° C. for aging and the other subgroup of thirty specimens was placed out in the open to be aged naturally. The oven conditioned samples were removed from the oven after 27, 60, 90, and 152 days of conditioning at 75° C.
Accelerating aging by oven conditioning the samples stimulates as much as possible the real world conditions of pavements. In the real world conditions, temperature of a pavement layer decreases with increasing depth from the surface. By encasing the test samples in PVC sleeves, this would prevent oxygen from moving through the sidewalls of the samples and thereby stimulate a real world condition for pavements.
Tables 1 through 5 summarize the data obtained by testing binder samples recovered from top ½ inch layer of the compacted mixture specimens for the untreated, CQS emulsion, and CQS emulsion produced from asphalt containing 5% of plant sterols.
Table 1 is the base or control data for all the treatments. Table 1 data was recovered from a compacted mix specimen, which received no treatment and had not been aged.
TABLE 1
Properties of Recovered Binder with no Treatment and no Aging
Properties Of Recovered Binder From Sample With No Aging
PG PG S- m-
Grade Grade critical critical
Sample @ 1.0 kPa, @ 2.2 kPa, Temp, Temp, ΔTc, R-
ID Description ° C. ° C. ° C. ° C. ° C. Value
Control control, Top 87.1 80.5 −29.74 −28.62 −1.13 2.621
0.5″, T-30, P-15,
Rec AC, 4 mm,
HR3-4 no aging
The data in Tables 2 through 5 summarize the recovered binder data after 27, 60, 90, and 152 days of aging at 75° C. in a forced draft oven. Both the PG Grade at 1.0 kPa and 2.2 kPa provide an indication of the relative change in binder stiffness. The higher the temperature at which the binder achieves a stiffness of 1.0 kPa or 2.2 kPa the more aged that binder has become. The low temperature Stiffness Critical temperature (S-critical) and the relaxation critical temperature (m-critical) track the change in the low temperature grade of the recovered binder. These values were determined using a 4 mm dynamic shear rheometer test following the procedure of Sui, et al. referenced in this application. The parameter labeled ΔTc is determined by subtracting the m-critical value from the S-critical value. The more negative the ΔTc result becomes the more susceptible to fatigue cracking the mixture containing that binder becomes. Values of ΔTc less than −5° C. for a binder are indicative of mixture susceptible to fatigue cracking. The R-value parameter is an indication of the ability of a binder to relax stress. Binders with higher R-values have more trouble relaxing stress and consequently are more prone to cracking.
TABLE 2
Properties of Recovered Binder from the top ½ inch of the compacted specimens for all
Treatments after 27 Days of Aging at 75° C.
Properties Of Recovered Binder After 27 Days Mix Aging @ 75° C.
S- m-
PG Grade PG Grade critical critical
Sample @ 1.0 kPa, @ 2.2 kPa, Temp, Temp, ΔTc, R-
ID Description ° C. ° C. ° C. ° C. ° C. Value
1 Untreated, 27 days at 89.8 83.8 −28.32 −25.05 −3.27 2.802
75°, T-1, P-33, Top
0.5″, Rec AC, 4 mm,
HR3-4-2
2 CQS−No Sterol, 27 85.9 79.7 −29.03 −27.39 −1.64 2.532
days at 75°, T-5, P-3,
Top 0.5″, Rec AC,
4 mm, HR3-4
3 CQS+Sterol, 27 days 84.3 77.9 −28.77 −28.24 −0.53 2.283
at 75°, T-7, P-19, Top
0.5″, Rec AC, DSR,
HR3-3
TABLE 3
Properties of Recovered Binder from the top ½ inch of the compacted specimens for all
Treatments after 60 Days of Aging at 75° C.
Properties Of Recovered Binder After 60 Days Mix Aging @ 75° C.
S- m-
PG Grade PG Grade critical critical
sample @ 1.0 kPa, @ 2.2 kPa, Temp, Temp, ΔTc, R-
ID Description ° C. ° C. ° C. ° C. ° C. Value
4 Untreated, 60 days@ 92.8 86.4 −25.65 −19.96 −5.69 3.098
75° C., T-11, P-29,
Top 0.5″, 4 mm, HR3-2
5 CQS−No Sterol 60 93.1 87.0 −26.80 −20.35 −6.46 3.008
days@ 75° C., T-13, P-
11, Top 0.5″, 4 mm,
HR3-3 (1)
6 CQS+Sterol, 60 91.0 84.8 −26.96 −23.42 −3.54 2.720
days@ 75° C., T-19, P-
20, Top 0.5″, 4 mm,
HR3-3 (1)
TABLE 4
Properties of Recovered Binder from the top ½ inch of the compacted specimens for all
Treatments after 90 Days of Aging at 75° C.
Properties Of Recovered Binder After 90 Days Mix Aging @ 75° C.
m-
PG Grade PG Grade S-critical critical
sample @ 1.0 kPa, @ 2.2 kPa, Temp, Temp, ΔTc, R-
ID Description ° C. ° C. ° C. ° C. ° C. Value
7 Untreated 90 Days 101.6 95.2 −24.99 −17.09 −7.89 3.304
@75° C., T15&P7, Top
0.5″, 4 mm, HR3-2 T-
avg
8 CQS− No Sterol, 90 97.9 91.4 −25.06 −18.38 −6.67 3.125
days @ 75° C., T-8, P-
16, Top 0.5″, Rec AC,
4 mm, HR3-1 T-avg
9 CQS+ sterol, 90 days 98.1 91.2 −23.96 −19.07 −4.89 2.939
@ 75° C., T-21, P-25,
Top 0.5″, Rec AC,
4 mm, HR3-1 T-avg
TABLE 5
Properties of Recovered Binder from the top 1/2 inch of the compacted specimens for all
Treatments after 152 Days of Aging at 75° C.
Properties Of Recovered Binder After 152 Days Mix Aging @ 75° C.
S- m-
PG Grade PG Grade critical critical
Sample @ 1.0 kPa, @ 2.2 kPa, Temp, Temp, ΔTc, R-
ID Description ° C. ° C. ° C. ° C. ° C. Value
10 Untreated 152 Days 118.8 111.8 −20.57 −5.66 −14.91 3.943
@75° C.,
T24&P10, Top 0.5″,
4 mm, HR3-2 T-avg
11 CQS− No Sterol, 152 111.4 104.5 −21.92 −10.09 −11.83 3.658
days @ 75° C., T-23,
P-18, Top 0.5″, Rec
AC, 4 mm, HR3-2 T-
avg
12 CQS+ sterol, 152 108.6 101.9 −21.95 −12.81 −9.14 3.299
days @ 75° C., T-28,
P-27, Top 0.5″, Rec
AC, 4 mm, HR3-1 T-
avg
The data summarized in these tables show that the binders recovered from the specimens treated with the CQS emulsion produced from the base binder with 5% sterol have the lowest values of m-critical temperatures, the least negative values of ΔTc and lowest R-values compared to the other two treatments. At every aging step the sterol containing treatment retarded the impact of aging resulting from conditioning temperature and oxidative hardening.
FIGS. 2 to 6 show the data from Tables 1 through 5 plotted for easier interpretation. For aged asphalt binders the low temperature m-critical value (FIG. 2 ) is the low temperature PG grade of the binder. The m-critical temperature is obtained from the slope measured at 60 seconds of the relaxation modulus master curve. The m-critical slope value can be obtained from the Bending Beam Rheometer or test (ASTM D6648) or from the 4 mm DSR test as shown by the research of Sui and Farrar at Western Research Institute. The more readily a binder can relax stresses the lower will be binder failing temperature. The sterol addition showed improving the ability of the binder to relax stresses at low and intermediate temperatures.
FIG. 3 is a plot of the low temperature S-critical or Stiffness Critical value at the different aging times. FIG. 3 shows that there is minor variation in the S-critical values between treatments at any given aging time. It is also worth emphasizing that although the S-critical temperatures are colder than the m-critical temperatures the PG binder specifications for the low temperature failing grade of the binder is based on the warmer of these two low temperature values. Therefore, if an additive can slow down the rate at which the m-critical value degrades then the binder will have better low temperature performance.
FIG. 4 is a plot of the ΔTc value at the different aging times. FIG. 4 shows that initially (at 27 days) the addition of both the CQS and CQS+sterol emulsions to the mix specimens improved the ΔTc values for those two treatments relative to the original ΔTc at zero time. The recovered binder for the untreated samples shows that ΔTc decreased by more than 2° C., whereas ΔTc for the plain CQS treated samples decreased only about 0.5° C. The ΔTc value for the CQS+sterol treated samples increased by 0.6° C. The additional asphalt binder added to the original specimens accounted for a reduced rate of aging for the CQS treated specimens and the additional asphalt binder plus the impact of the sterol accounted for the improvement of the recovered binder after 27 days of aging relative to the ΔTc of zero-day aged mix. After both 60 and 90 days of aging the ΔTc values of binder recovered from the CQS+sterol treated specimens were still greater than −5° compared to ΔTc for the untreated and CQS treated specimens. Even after 152 days of aging the CQS+sterol treated specimens have a better ΔTc value compared to the other treatments.
FIG. 5 is a plot of the binder Rheological index or R-Value for the different treatments. The R-value is another indicator of the ability of a binder to relax stress. Binders with increasing R-Values have decreased ability to relax stress. It is desirable to keep R-Value under 3 and as FIG. 5 shows the initial application of the emulsion treatments reduced the R-values for those two treatments, but by 60 hours of aging the untreated and CQS treated specimens had values greater than 3. Through the entire aging sequence, the CQS+sterol treated specimens had consistently better R-values than the other treatments.
FIG. 6 is a plot of the high temperature PG grade of binders recovered from the various treatments with aging time. The data shows relatively minor variation in high temperature grade with aging; however, the CQS+sterol treatment does consistently have the lowest high temperature value. The high temperature property of the binder is not highly significant as long as the binder is stiff enough to resist rutting and for a typical upper Midwestern US climate, all of these binders possess sufficient stiffness.
Tables 6 and 7 show the properties of binders recovered from the 2nd ½ inch of the compacted specimens after 60 and 152 days of aging. The purpose of obtaining this data at these intervals was to show the aging of the binder in these layers compared to aging of the binder in the top ½ inch mixture layers. With the exception of the ΔTc value for the 2nd ½ inch binder from the untreated specimen the properties of these recovered binders at 60 days and at 152 days are similar. The 60 day untreated sample with a ΔTc of −3.80° C. may be due to the warmer S-critical value for the untreated sample compared to the CQS and CQS+sterol treatments. A warmer S-critical value indicates a greater aging of the stiffness failure temperature compared to the treated samples and could be due to more oxygen migration into the 2nd ½ inch of the mix. Because the untreated samples did not have any emulsion treatment, the surface half inch of those untreated specimens would have a greater opportunity for oxygen to permeate the mix. The R-value for the untreated 60 day recovered binder is similar to the other two treatments which is consistent with similar properties of relaxation and also consistent with the similarities of the m-critical properties of all three treatments for the 2nd ½ inch recovered binders.
FIG. 7 shows bar chart comparisons of the S-critical and m-critical data between the top ½ inch and second ½ inch recovered binder at 60 days of aging. FIG. 8 shows comparison between the ΔTc and R-Value properties for the same binders at 60 days of aging. FIGS. 9 and 10 show similar respective plots for the binders recovered from the top and second ½ inch of binders recovered after 152 days of aging.
The S-critical values show hardly any variation with respect to depth for any treatment and the m-critical value for the top ½ inch of the CQS+sterol treatment exhibits a 2.4° C. better low temperature m-critical value than the binder from the 2nd half inch. The fact that the CQS treated specimens exhibited an m-critical value 0.6° C. better than the second half inch recovered binder shows that the additional binder added to the mix was not the source of the more greatly improved m-critical value in the CQS+sterol specimens and shows that the fog seal application of the emulsion containing the sterol resides in the top half inch layer.
The data plotted in FIG. 8 shows ΔTc values for the top half inch and second half inch binders after 60 days. The R-value for the top half inch of the sterol treated mix was also lower than the second half inch.
FIG. 9 shows S-critical and m-critical comparisons after 152 days of aging. The S-critical data is very similar for all treatments for both layers. The m-critical values show definite differences. The second half inch layers were very similar with the untreated specimens having a slightly warmer m-critical temperature. The CQS treated specimens had a m-critical value 2.67° C. cooler (i.e. better) for the top half inch compared to the second half inch (−10.09° C. vs. −7.42° C.). This is attributable to the extra asphalt added in the fog seal. The top half inch of the CQS+sterol however had an m-critical value that was 2.7° C. cooler (i.e. better) than the CQS only treatment and 5.7° C. cooler (i.e. better) than the second layer of the CQS+sterol treatment specimens. This shows that sterol treated specimens resides in the top half inch. The CQS treated results also show that the fog seal treatment in general resides in the top half inch while at the same time emphasizing that just applying the asphalt emulsion does not provide the same age retarding benefits as having the sterol additive present in the treatment.
FIG. 10 compares the ΔTc and R-values for the three treatments after 152 days of conditioning. The ΔTc values for both layers of the untreated specimens and the second half-inch of the CQS and CQS+sterol treatments are all similar with the emulsion treated specimens being slightly better, most likely due to the asphalt added to the surface of those specimens. The CQS treated specimens had a top half-inch layer ΔTc 2.2° C. better than the second half-inch binder, but the CQS+sterol top half inch layer ΔTc was 5° C. better than the second half inch layer. The R-value data also shows similar relative performance. The untreated specimens have nearly identical R-values, the CQS treated specimens show that the top half inch binder has a 0.25 R-value improvement over the second half inch binder and the CQS+sterol treated specimens have a top half inch binder has a 0.74 R-value improvement over the binder in the second half inch.

Claims (16)

What is claimed is:
1. A method for slowing the aging rate of an existing asphalt-containing pavement comprising:
applying a sterol-containing asphalt binder emulsion to the surface of the existing asphalt-containing pavement; wherein the asphalt binder emulsion comprises asphalt binder and 0.5 to 15 wt. % of a sterol additive based on the asphalt binder weight; and
curing the applied sterol-containing asphalt binder emulsion to form a surface treatment on the existing asphalt-containing pavement, said surface treatment comprising the sterol additive, wherein the sterol additive in the surface treatment retards or slows the aging rate of the underlying existing asphalt-containing pavement, and wherein the sterol additive comprises a sterol blend of 10:90 ratio by weight to 90:10 ratio by weight of pure sterol:crude sterol.
2. The method of claim 1, wherein the sterol additive is 1 to 10 wt. % of the asphalt binder weight.
3. The method of claim 1, wherein the sterol additive comprises cholesterol.
4. The method of claim 3, wherein the pure sterol comprises a blend of plant sterol and cholesterol.
5. The method of claim 1, wherein the crude sterol additive comprises a plant sterol source.
6. The method of claim 5, wherein the crude sterol source comprises a tall oil pitch.
7. The method of claim 1, wherein the existing pavement comprises reclaimed asphalt binder from recycled asphalt pavement (RAP), recycled asphalt shingles (RAS), a softening agent, or combinations thereof.
8. The method of claim 1, wherein the sterol-containing asphalt binder provides a ΔTc of greater than or equal to −5.0° C.
9. A road surface made from the method of claim 1.
10. The method of claim 1, wherein the surface treatment is applied as the asphalt binder component of a chip seal layer.
11. The method of claim 1, wherein the surface treatment is applied as a fog seal.
12. The method of claim 1, wherein the surface treatment is applied as a tack coat.
13. The method of claim 1, wherein the surface treatment reduces surface cracking of the existing asphalt pavement or reduces moisture uptake of the existing asphalt pavement.
14. The method of claim 1, wherein the sterol-containing asphalt binder emulsion is applied to the surface of the existing pavement as an asphalt binder component of a thinlay having a thickness of about 12 mm (0.5 inches) to about 38 mm (1.5 inches).
15. The method of claim 1, wherein the surface treatment is applied to the surface of the existing pavement as an asphalt binder component of a thinlay having a thickness of 12 mm (0.5 inches) to about 19 (0.75 inches) mm.
16. The method of claim 1, wherein the sterol additive comprises campesterol, stigasterol, stigmasterol, β-sitosterol, Δ5-avenosterol, Δ7-stigasterol, Δ7-avenosterol, brassicasterol or mixtures thereof.
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US16/757,697 US11718756B2 (en) 2017-10-20 2018-10-11 Asphalt emulsion surface treatment containing sterol
EP18795903.6A EP3697849A1 (en) 2017-10-20 2018-10-11 Asphalt emulsion surface treatment containing sterol
MX2020003711A MX2020003711A (en) 2017-10-20 2018-10-11 Asphalt emulsion surface treatment containing sterol.
AU2018350814A AU2018350814A1 (en) 2017-10-20 2018-10-11 Asphalt emulsion surface treatment containing sterol
CR20200164A CR20200164A (en) 2017-10-20 2018-10-11 Asphalt emulsion surface treatment containing sterol
BR112020007768-2A BR112020007768A2 (en) 2017-10-20 2018-10-11 sterol-containing asphalt emulsion surface treatment
CN201880083286.0A CN111902487A (en) 2017-10-20 2018-10-11 Sterol-containing asphalt emulsion surface treatment
PCT/US2018/055443 WO2019079101A1 (en) 2017-10-20 2018-10-11 Asphalt emulsion surface treatment containing sterol
JP2020522056A JP2021500496A (en) 2017-10-20 2018-10-11 Sterol-containing asphalt emulsion surface treatment
CA3079097A CA3079097A1 (en) 2017-10-20 2018-10-11 Asphalt emulsion surface treatment containing sterol
ZA2020/02127A ZA202002127B (en) 2017-10-20 2020-05-04 Asphalt emulsion surface treatment containing sterol
US18/086,231 US20230128467A1 (en) 2017-02-02 2022-12-21 Sterol additive in asphalt pavement
US18/209,922 US20230323126A1 (en) 2017-10-20 2023-06-14 Asphalt emulsion surface treatment containing sterol

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Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6998369B2 (en) 2016-06-10 2022-02-10 エー.エル.エム.ホールディング カンパニー How to determine the degree of aging on asphalt
ES2832477T3 (en) 2016-08-09 2021-06-10 Alm Holding Co Sterol mixtures as an additive in asphalt binder
EP3577169A1 (en) 2017-02-02 2019-12-11 A.L.M. Holding Company Bituminous emulsions containing sterol additive for asphalt pavement
US11427697B2 (en) 2017-07-26 2022-08-30 A.L.M. Holding Company Use of sterols from animal waste as an additive in asphalt binder
MX2020003711A (en) * 2017-10-20 2020-10-05 Alm Holding Co Asphalt emulsion surface treatment containing sterol.
CN109574551A (en) * 2019-01-28 2019-04-05 上海时申工贸有限公司 A kind of environment-friendly type regeneration bituminous concrete and its preparation process
US10851500B2 (en) * 2019-04-23 2020-12-01 Manhole Adjusting Inc. Recycled asphalt compositions and methods thereof
WO2021011704A1 (en) 2019-07-15 2021-01-21 A.L.M Holding Company Sterol in asphalt roofing materials
EP3999589A1 (en) * 2019-07-15 2022-05-25 A.L.M. Holding Company Recycling of sterol-containing asphalt binder
WO2021141635A1 (en) * 2020-01-08 2021-07-15 Adventus Material Strategies, Llc Crack sealant method and composition for reduced color contrast
US11760881B1 (en) * 2020-01-08 2023-09-19 Adventus Material Strategies, Llc Crack sealant method and composition for resistance to UV aging and weathering
WO2022036131A1 (en) 2020-08-14 2022-02-17 Building Materials Investment Corporation Non-asphaltic coatings, non-asphaltic roofing materials, and methods of making the same
AU2022268264A1 (en) 2021-04-26 2023-11-09 A.L.M. Holding Company Age rate retarding additives for asphalt binders
CN113897836A (en) * 2021-09-29 2022-01-07 陕西交通职业技术学院 Nano toughened rubber asphalt open road surface structure and construction method thereof
CN116903297B (en) * 2023-07-20 2024-03-22 聊城市交通发展有限公司 Warm mix asphalt mixture containing reclaimed materials and preparation method thereof

Citations (66)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1112492A (en) 1904-09-07 1914-10-06 Westinghouse Air Brake Co Lubricator for air-pumps.
US2280843A (en) 1940-09-30 1942-04-28 Newport Ind Inc Method of concentrating the sterol content of tall oil
US2286244A (en) * 1940-12-09 1942-06-16 Standard Oil Co Asphalt preparation
US2392863A (en) * 1940-11-20 1946-01-15 Standard Oil Co Asphalt preparation
GB575484A (en) * 1943-08-04 1946-02-20 Fred Dawson Construction of aircraft runways, roads, floors and like surfaces, and manufacture of water-repellent materials therefor
US2411634A (en) * 1945-05-19 1946-11-26 Howard B Bishop Bituminous paved surface and method of making the same
US2585336A (en) * 1948-06-14 1952-02-12 American Bitumuls & Asphalt Co Quick-breaking bituminous emulsion
US2715638A (en) 1953-07-28 1955-08-16 American Cyanamid Co Production of sterols from tall oil pitch
US2793138A (en) 1956-04-20 1957-05-21 Texas Co Coating wet metal surfaces with asphalt cutback compositions
US2860067A (en) * 1954-08-09 1958-11-11 Standard Oil Co Roadway construction material and an additive therefor
US3032507A (en) * 1959-09-02 1962-05-01 California Research Corp Cationic bituminous emulsions
US3691211A (en) 1970-12-07 1972-09-12 Procter & Gamble Process for preparing sterols from tall oil pitch
US3926936A (en) 1972-11-17 1975-12-16 Oulo Osakeyhtio Process for manufacturing valuable products from tall oil pitch
US3951676A (en) 1971-07-14 1976-04-20 Chevron Research Company Cationic bituminous emulsions forming residuum having improved temperature characteristics
US4044031A (en) 1976-07-02 1977-08-23 Ake Allan Johansson Process for the separation of sterols
US4874432A (en) * 1988-06-27 1989-10-17 Asphalt Materials, Inc. Multigrade asphalt cement product and process
US5437717A (en) * 1994-06-13 1995-08-01 Vinzoyl Petroleum Co. Asphalt compositions with improved cross-linking agent
US5473000A (en) * 1991-11-18 1995-12-05 O. Pinomaa Ky Method for improving the strength of bitumen, asphalt or a similar material, and a composition obtained by the method
US5496400A (en) * 1994-06-13 1996-03-05 Vinzoyl Petroleum Co. Asphalt compositions with improved cross-linking agent
US6057462A (en) 1998-11-06 2000-05-02 Westvaco Corporation Isolation and purification of sterols from neutrals fraction of tall oil pitch by single decantation crystallization
WO2001072315A1 (en) 2000-03-28 2001-10-04 Birken Gmbh Emulsion containing a plant extract, method for producing said emulsion and for obtaining a plant extract
US20030144536A1 (en) 2002-01-28 2003-07-31 Forbes Medi-Tech Inc. Process of extracting and purifying phytosterols and phytostanols from tall oil pitch
WO2004016336A1 (en) 2002-08-14 2004-02-26 Birken Gmbh Device and method for continuously extracting extract materials from solid materials, for washing solid materials and recrystallizing
US6770127B2 (en) * 2002-05-16 2004-08-03 Shandong Heritage Highway Materials Technologies Multigrade asphalt power additive
JP2005154465A (en) 2003-11-20 2005-06-16 Nippon Oil Corp Reclaiming additive composition for asphalt pavement waste material
US6987207B1 (en) 2005-03-03 2006-01-17 Alan Jeffrey Ronyak Hydrocarbonaceous composition
EP1728831A1 (en) 2005-06-03 2006-12-06 Nederlandse Organisatie voor toegepast-natuurwetenschappelijk Onderzoek TNO Bitumen composition with improved ageing resistance
US20070122235A1 (en) 2004-12-03 2007-05-31 Green Arm Co., Ltd. Method for continuous on-site recycling of an asphalt mixture layer of a pavement and a motor-driven vehicle system therefor
US20070151480A1 (en) 2002-05-02 2007-07-05 Archer-Daniels-Midland Company Hydrogenated and partially hydrogenated heat-bodied oils and uses thereof
US7575767B2 (en) * 2002-08-20 2009-08-18 Malaysian Palm Oil Board Extraction of palm vitamin E, phytosterols and squalene from palm oil
US20100170417A1 (en) 2009-01-08 2010-07-08 De Sil Va Resources, Llc A Texas Corporation Cutback asphalt compositions and products comprising an extender derived from tall oil, and methods for making and using same
US20100190892A1 (en) 2009-01-26 2010-07-29 Carlisle Intangible Company Highly-filled sealant compositions
WO2010110651A1 (en) 2009-03-24 2010-09-30 Van Weezenbeek Specialties B.V. Method for rejuvenating a bitumen containing composition
US7811372B2 (en) 2007-01-08 2010-10-12 Shell Oil Company Rejuvenating agent and process for recycling of asphalt
WO2010128105A1 (en) 2009-05-07 2010-11-11 Shell Internationale Research Maatschappij B.V. Binder composition and asphalt mixture
US20100305342A1 (en) 1998-02-20 2010-12-02 Alfred Wong Method for the prepparation of phytosterols from tall oil pitch
US20100319577A1 (en) 2007-11-14 2010-12-23 Akzo Nobel N.V. Asphalt modifiers for "warm mix" applications including adhesion promoter
US20120060722A1 (en) * 2009-05-19 2012-03-15 Total Raffinage Marketing Bituminous binder for preparing low-temperature asphalt or coated materials
JP2012093108A (en) 2010-10-25 2012-05-17 Sumitomo Rubber Ind Ltd Method of predicting friction coefficient
WO2013090283A1 (en) 2011-12-12 2013-06-20 Arizona Chemical Company, Llc Rejuvenation of reclaimed asphalt
WO2013163467A1 (en) 2012-04-26 2013-10-31 Arizona Chemical Company, Llc Rejuvenation of reclaimed asphalt
CN103387749A (en) 2013-07-16 2013-11-13 交通运输部公路科学研究所 A vegetable oil-type asphalt recycling agent and a method for preparing the same
WO2014047462A1 (en) 2012-09-21 2014-03-27 North Carolina Agricultural And Technical State University Preparation and uses of bio-adhesives
US8696806B2 (en) * 2009-05-01 2014-04-15 Iowa State University Research Foundation, Inc. Asphalt materials containing bio-oil and methods for production thereof
US8741052B2 (en) * 2007-07-26 2014-06-03 Akzo Nobel N.V. Adhesion and cohesion modifiers for asphalt
US20140234027A1 (en) * 2013-02-20 2014-08-21 Ergon Asphalt & Emulsions, Inc. Acrylic-modified asphalt rejuvenating emulsion
US20150087753A1 (en) * 2013-09-23 2015-03-26 Western Emulsions, Inc. Modified asphalt paving composition
WO2015070180A1 (en) 2013-11-11 2015-05-14 Collaborative Aggregates, Llc Novel asphalt binder additive compositions and methods of use
CN104629392A (en) 2015-03-06 2015-05-20 西安公路研究院 Environment-friendly type high-permeability emulsified asphalt based on plant asphalt
US20150329702A1 (en) 2012-12-11 2015-11-19 Korea Institute Of Construction Technology Warm mix recycled asphalt additive containing oil dregs, and warm mix recycled asphalt mixture containing same
WO2016065270A1 (en) * 2014-10-23 2016-04-28 Cargill, Incorporated Imidazoline functionalized oxidized fatty substance emulsifiers and methods
US20160122507A1 (en) 2014-11-03 2016-05-05 Flint Hills Resources, Lp Asphalt binders containing a glyceride and fatty acid mixture and methods for making and using same
US20160160453A1 (en) * 2014-05-06 2016-06-09 Donelson Construction Co., Llc Surfacing system and method
US20160362338A1 (en) * 2015-06-10 2016-12-15 Alm Holding Company Use of sterols as an additive in asphalt binder
WO2017011747A1 (en) 2015-07-15 2017-01-19 Ergon Asphalt & Emulsions, Inc. Biobased asphalt rejuvenating emulsion
CA3026997A1 (en) * 2016-06-10 2017-12-14 A.L.M. Holding Company A method for identifying the extent of aging in an asphalt
US20170370899A1 (en) 2016-06-22 2017-12-28 Arizona Chemical Company, Llc Methods for Evaluating Asphalt Mix Compositions Containing Reclaimed Asphalt
WO2018031540A1 (en) 2016-08-09 2018-02-15 A.L.M Holding Company Sterol blends as an additive in asphalt binder
US20180171146A1 (en) 2016-12-19 2018-06-21 Blacklidge Emulsions Inc. Age-resistant asphalt compositions and methods
US20180215919A1 (en) 2017-02-02 2018-08-02 A.L.M Holding Company Sterol additive in asphalt pavement
WO2019023172A1 (en) 2017-07-26 2019-01-31 A.L.M Holding Company Use of sterols from animal waste as an additive in asphalt binder
US20190152850A1 (en) 2013-11-11 2019-05-23 Collaborative Aggregates, Llc Novel Asphalt Binder Additive Compositions and Methods of Use
US20200277497A1 (en) * 2017-10-20 2020-09-03 A.L.M. Holding Company Asphalt emulsion surface treatment containing sterol
US10793720B2 (en) * 2017-03-20 2020-10-06 Kraton Polymers U.S. Llc Reclaimed asphalt composition and methods of making and using same
US10961395B2 (en) * 2016-02-29 2021-03-30 Iowa State University Research Foundation, Inc. Rejuvenation of vacuum tower bottoms through bio-derived materials
US11124926B2 (en) * 2018-02-02 2021-09-21 Kraton Polymers Llc Pavement repair method and system thereof

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2728682A (en) * 1952-06-18 1955-12-27 Standard Oil Co Asphalt compositions
US3044373A (en) * 1958-02-20 1962-07-17 Straba Handels Ag Bituminous surfaces
CN104559248B (en) * 2013-10-22 2017-02-22 中国石油化工股份有限公司 Cationic pitch warm mixing agent and preparation method thereof
FR3035112B1 (en) * 2015-04-14 2020-05-29 Soprema PLANT-BASED BINDER, COMPOSITIONS COMPRISING THE SAME, AND METHOD FOR REDUCING THE QUANTITY OF OIL BITUMEN

Patent Citations (96)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1112492A (en) 1904-09-07 1914-10-06 Westinghouse Air Brake Co Lubricator for air-pumps.
US2280843A (en) 1940-09-30 1942-04-28 Newport Ind Inc Method of concentrating the sterol content of tall oil
US2392863A (en) * 1940-11-20 1946-01-15 Standard Oil Co Asphalt preparation
US2286244A (en) * 1940-12-09 1942-06-16 Standard Oil Co Asphalt preparation
GB575484A (en) * 1943-08-04 1946-02-20 Fred Dawson Construction of aircraft runways, roads, floors and like surfaces, and manufacture of water-repellent materials therefor
US2411634A (en) * 1945-05-19 1946-11-26 Howard B Bishop Bituminous paved surface and method of making the same
US2585336A (en) * 1948-06-14 1952-02-12 American Bitumuls & Asphalt Co Quick-breaking bituminous emulsion
US2715638A (en) 1953-07-28 1955-08-16 American Cyanamid Co Production of sterols from tall oil pitch
US2860067A (en) * 1954-08-09 1958-11-11 Standard Oil Co Roadway construction material and an additive therefor
US2793138A (en) 1956-04-20 1957-05-21 Texas Co Coating wet metal surfaces with asphalt cutback compositions
US3032507A (en) * 1959-09-02 1962-05-01 California Research Corp Cationic bituminous emulsions
US3691211A (en) 1970-12-07 1972-09-12 Procter & Gamble Process for preparing sterols from tall oil pitch
US3951676A (en) 1971-07-14 1976-04-20 Chevron Research Company Cationic bituminous emulsions forming residuum having improved temperature characteristics
US3926936A (en) 1972-11-17 1975-12-16 Oulo Osakeyhtio Process for manufacturing valuable products from tall oil pitch
US4044031A (en) 1976-07-02 1977-08-23 Ake Allan Johansson Process for the separation of sterols
US4874432A (en) * 1988-06-27 1989-10-17 Asphalt Materials, Inc. Multigrade asphalt cement product and process
US5473000A (en) * 1991-11-18 1995-12-05 O. Pinomaa Ky Method for improving the strength of bitumen, asphalt or a similar material, and a composition obtained by the method
US5496400A (en) * 1994-06-13 1996-03-05 Vinzoyl Petroleum Co. Asphalt compositions with improved cross-linking agent
US5437717A (en) * 1994-06-13 1995-08-01 Vinzoyl Petroleum Co. Asphalt compositions with improved cross-linking agent
US20100305342A1 (en) 1998-02-20 2010-12-02 Alfred Wong Method for the prepparation of phytosterols from tall oil pitch
US6057462A (en) 1998-11-06 2000-05-02 Westvaco Corporation Isolation and purification of sterols from neutrals fraction of tall oil pitch by single decantation crystallization
WO2001072315A1 (en) 2000-03-28 2001-10-04 Birken Gmbh Emulsion containing a plant extract, method for producing said emulsion and for obtaining a plant extract
US20030087789A1 (en) 2000-03-28 2003-05-08 Scheffler Armin Emulsion containing a plant extract, method for producing said emulsion and for obtaining a plant extract
US20030144536A1 (en) 2002-01-28 2003-07-31 Forbes Medi-Tech Inc. Process of extracting and purifying phytosterols and phytostanols from tall oil pitch
US20070151480A1 (en) 2002-05-02 2007-07-05 Archer-Daniels-Midland Company Hydrogenated and partially hydrogenated heat-bodied oils and uses thereof
US6770127B2 (en) * 2002-05-16 2004-08-03 Shandong Heritage Highway Materials Technologies Multigrade asphalt power additive
WO2004016336A1 (en) 2002-08-14 2004-02-26 Birken Gmbh Device and method for continuously extracting extract materials from solid materials, for washing solid materials and recrystallizing
US7575767B2 (en) * 2002-08-20 2009-08-18 Malaysian Palm Oil Board Extraction of palm vitamin E, phytosterols and squalene from palm oil
JP2005154465A (en) 2003-11-20 2005-06-16 Nippon Oil Corp Reclaiming additive composition for asphalt pavement waste material
US20070122235A1 (en) 2004-12-03 2007-05-31 Green Arm Co., Ltd. Method for continuous on-site recycling of an asphalt mixture layer of a pavement and a motor-driven vehicle system therefor
US7448825B2 (en) 2004-12-03 2008-11-11 Green Arm Co., Ltd. Method for continuous on-site recycling of an asphalt mixture layer of a pavement and a motor-driven vehicle system therefor
US6987207B1 (en) 2005-03-03 2006-01-17 Alan Jeffrey Ronyak Hydrocarbonaceous composition
EP1728831A1 (en) 2005-06-03 2006-12-06 Nederlandse Organisatie voor toegepast-natuurwetenschappelijk Onderzoek TNO Bitumen composition with improved ageing resistance
US7811372B2 (en) 2007-01-08 2010-10-12 Shell Oil Company Rejuvenating agent and process for recycling of asphalt
US8741052B2 (en) * 2007-07-26 2014-06-03 Akzo Nobel N.V. Adhesion and cohesion modifiers for asphalt
US20100319577A1 (en) 2007-11-14 2010-12-23 Akzo Nobel N.V. Asphalt modifiers for "warm mix" applications including adhesion promoter
US20100170417A1 (en) 2009-01-08 2010-07-08 De Sil Va Resources, Llc A Texas Corporation Cutback asphalt compositions and products comprising an extender derived from tall oil, and methods for making and using same
US20100190892A1 (en) 2009-01-26 2010-07-29 Carlisle Intangible Company Highly-filled sealant compositions
WO2010110651A1 (en) 2009-03-24 2010-09-30 Van Weezenbeek Specialties B.V. Method for rejuvenating a bitumen containing composition
US8696806B2 (en) * 2009-05-01 2014-04-15 Iowa State University Research Foundation, Inc. Asphalt materials containing bio-oil and methods for production thereof
US8513338B2 (en) 2009-05-07 2013-08-20 Shell Oil Company Binder composition and asphalt mixture
CL2011002791A1 (en) 2009-05-07 2012-04-20 Shell Int Research Binder composition comprising a resin of vegetable origin, an oil of vegetable origin and a polymer in which the polymer is functionalized with silane groups; aqueous emulsion; and asphalt mix.
WO2010128105A1 (en) 2009-05-07 2010-11-11 Shell Internationale Research Maatschappij B.V. Binder composition and asphalt mixture
US20120060722A1 (en) * 2009-05-19 2012-03-15 Total Raffinage Marketing Bituminous binder for preparing low-temperature asphalt or coated materials
JP2012093108A (en) 2010-10-25 2012-05-17 Sumitomo Rubber Ind Ltd Method of predicting friction coefficient
WO2013090283A1 (en) 2011-12-12 2013-06-20 Arizona Chemical Company, Llc Rejuvenation of reclaimed asphalt
WO2013163467A1 (en) 2012-04-26 2013-10-31 Arizona Chemical Company, Llc Rejuvenation of reclaimed asphalt
US10030145B2 (en) * 2012-04-26 2018-07-24 Kraton Chemical, Llc Rejuvenation of reclaimed asphalt
WO2013163463A1 (en) 2012-04-26 2013-10-31 Arizona Chemical Company, Llc Rejuvenation of reclaimed asphalt
US20140338565A1 (en) * 2012-04-26 2014-11-20 Arizona Chemical Company, Llc Rejuvenation of reclaimed asphalt
CN104245850A (en) 2012-04-26 2014-12-24 阿利桑那化学公司 Rejuvenation of reclaimed asphalt
CN104364318A (en) 2012-04-26 2015-02-18 阿利桑那化学公司 Rejuvenation of reclaimed asphalt
CL2014002871A1 (en) 2012-04-26 2015-07-10 Arizona Chemical Co Llc Asphaltic composition comprising regenerated asphalt and a rejuvenation agent with ester functionality derived from bogol oil or derived from at least one alcohol of improved thermal stability; rejuvenated binder; method; and paved surface.
US9828506B2 (en) 2012-04-26 2017-11-28 Kraton Chemical, Llc Rejuvenation of reclaimed asphalt
WO2014047462A1 (en) 2012-09-21 2014-03-27 North Carolina Agricultural And Technical State University Preparation and uses of bio-adhesives
US10077356B2 (en) 2012-09-21 2018-09-18 North Carolina Agricultural And Technical State University Preparation and uses of bio-adhesives
US20150329702A1 (en) 2012-12-11 2015-11-19 Korea Institute Of Construction Technology Warm mix recycled asphalt additive containing oil dregs, and warm mix recycled asphalt mixture containing same
JP2016509611A (en) 2012-12-11 2016-03-31 コリア インスティチュート オブ コンストラクション テクノロジー Medium temperature regenerated asphalt additive containing oil and fat residue and medium temperature regenerated asphalt mixture containing the same
US20140234027A1 (en) * 2013-02-20 2014-08-21 Ergon Asphalt & Emulsions, Inc. Acrylic-modified asphalt rejuvenating emulsion
CN103387749A (en) 2013-07-16 2013-11-13 交通运输部公路科学研究所 A vegetable oil-type asphalt recycling agent and a method for preparing the same
US20150087753A1 (en) * 2013-09-23 2015-03-26 Western Emulsions, Inc. Modified asphalt paving composition
US20190152850A1 (en) 2013-11-11 2019-05-23 Collaborative Aggregates, Llc Novel Asphalt Binder Additive Compositions and Methods of Use
WO2015070180A1 (en) 2013-11-11 2015-05-14 Collaborative Aggregates, Llc Novel asphalt binder additive compositions and methods of use
US9994485B2 (en) 2013-11-11 2018-06-12 Collaborative Aggregates, Llc Asphalt binder additive compositions and methods of use
US20160160453A1 (en) * 2014-05-06 2016-06-09 Donelson Construction Co., Llc Surfacing system and method
WO2016065270A1 (en) * 2014-10-23 2016-04-28 Cargill, Incorporated Imidazoline functionalized oxidized fatty substance emulsifiers and methods
US10167390B2 (en) 2014-11-03 2019-01-01 Flint Hills Resources, Lp Asphalt binders containing a glyceride and fatty acid mixture and methods for making and using same
WO2016073442A1 (en) 2014-11-03 2016-05-12 Flint Hills Resources, Lp Asphalt binders containing a glyceride and fatty acid mixture and methods for making and using same
US20160122507A1 (en) 2014-11-03 2016-05-05 Flint Hills Resources, Lp Asphalt binders containing a glyceride and fatty acid mixture and methods for making and using same
CA2965697A1 (en) * 2014-11-03 2016-05-12 Flint Hills Resources, Lp Asphalt binders containing a glyceride and fatty acid mixture and methods for making and using same
US9481794B2 (en) * 2014-11-03 2016-11-01 Flint Hills Resources, Lp Asphalt binders containing a glyceride and fatty acid mixture and methods for making and using same
CN104629392A (en) 2015-03-06 2015-05-20 西安公路研究院 Environment-friendly type high-permeability emulsified asphalt based on plant asphalt
WO2017027096A2 (en) 2015-06-10 2017-02-16 A.L.M Holding Company Use of sterols as an additive in asphalt binder
US20160362338A1 (en) * 2015-06-10 2016-12-15 Alm Holding Company Use of sterols as an additive in asphalt binder
US20180209102A1 (en) * 2015-07-15 2018-07-26 Ergon Asphalt & Emulsions, Inc. Biobased asphalt rejuvenating emulsion
WO2017011747A1 (en) 2015-07-15 2017-01-19 Ergon Asphalt & Emulsions, Inc. Biobased asphalt rejuvenating emulsion
US10961395B2 (en) * 2016-02-29 2021-03-30 Iowa State University Research Foundation, Inc. Rejuvenation of vacuum tower bottoms through bio-derived materials
US11168214B2 (en) * 2016-06-10 2021-11-09 A.L.M. Holding Company Method for identifying the extent of aging in an asphalt
US20190153229A1 (en) 2016-06-10 2019-05-23 A.L.M. Holding Co. Crude sterol as an additive in asphalt binder
US20190265221A1 (en) * 2016-06-10 2019-08-29 A.L.M. Holding Co. A method for identifying the extent of aging in an asphalt
WO2017213693A1 (en) 2016-06-10 2017-12-14 A.L.M Holding Company Crude sterol as an additive in asphalt binder
WO2017213692A1 (en) 2016-06-10 2017-12-14 A.L.M Holding Company A method for identifying the extent of aging in an asphalt
CA3026997A1 (en) * 2016-06-10 2017-12-14 A.L.M. Holding Company A method for identifying the extent of aging in an asphalt
US20170370899A1 (en) 2016-06-22 2017-12-28 Arizona Chemical Company, Llc Methods for Evaluating Asphalt Mix Compositions Containing Reclaimed Asphalt
WO2018031540A1 (en) 2016-08-09 2018-02-15 A.L.M Holding Company Sterol blends as an additive in asphalt binder
US10669202B2 (en) * 2016-08-09 2020-06-02 A.L.M. Holding Company Sterol blends as an additive in asphalt binder
US11097981B2 (en) * 2016-08-09 2021-08-24 A.L.M. Holding Company Sterol blends as an additive in asphalt binder
US20180171146A1 (en) 2016-12-19 2018-06-21 Blacklidge Emulsions Inc. Age-resistant asphalt compositions and methods
WO2018144731A1 (en) 2017-02-02 2018-08-09 A.L.M Holding Company Bituminous emulsions containing sterol additive for asphalt pavement
CN110799597A (en) 2017-02-02 2020-02-14 A.L.M控股公司 Asphalt emulsion containing sterol additive for asphalt pavement
US20180215919A1 (en) 2017-02-02 2018-08-02 A.L.M Holding Company Sterol additive in asphalt pavement
US10793720B2 (en) * 2017-03-20 2020-10-06 Kraton Polymers U.S. Llc Reclaimed asphalt composition and methods of making and using same
WO2019023172A1 (en) 2017-07-26 2019-01-31 A.L.M Holding Company Use of sterols from animal waste as an additive in asphalt binder
US20200207944A1 (en) 2017-07-26 2020-07-02 A.L.M. Holding Company Use of sterols from animal waste as an additive in asphalt binder
US20200277497A1 (en) * 2017-10-20 2020-09-03 A.L.M. Holding Company Asphalt emulsion surface treatment containing sterol
US11124926B2 (en) * 2018-02-02 2021-09-21 Kraton Polymers Llc Pavement repair method and system thereof

Non-Patent Citations (61)

* Cited by examiner, † Cited by third party
Title
"B-Sitosterol from Soybeans" downloaded from http://www.mpbio.com/product.php?pid=02102886, downloaded on May 21, 2015, 2 pages.
"Digging Into Asphaltenes", Sep. 21, 2009, vol. 87, No. 38, 7 pages, downloaded from http://pubs.acs.org/cen/coverstory/87/8738cover.html, downloaded on Jun. 5, 2011.
"Material Safety Data Sheet (Aug. 8, 2013), Sylfat.TM. DP8", Arizona Chemical Company LLC, 7 pages.
"Refining and Properties of Asphalt Binders", Asphalt Handbook, 7th Edition, 2007, 2 pages.
"Sylvaroad.TM. RP 1000 Performance Additive", Safety Data Sheet, Arizona Chemical Company LLC, Apr. 1, 2015, 7 pages.
"Tall Oil Fatty Acid", Ataman Kimya, retrieved on Aug. 10, 2021, 8 pages.
"Tallex Pitch", Ingevity Holdings SPRL, Safety Data Sheet, Jul. 21, 2017, 12 pages.
"Wood Chemistry PSE 406/Chem E 470", Lecture 13, Diterpenes and Triterpenes, Wood Chemistry, 5 pages.
Allen, et al. (2013) "Microstructural Characterization of the Chemo-Mechanical Behavior of Asphalt in Terms of Aging and Fatigue Performance Properties", UMI Dissertation Publishing, Proquest LLC., 162 pages.
Amy Epps Martin et al, The Effects of Recycling Agents on Asphalt Mixtures with High RAS and RAP Binder Ratios (Project N 9-58), Mar. 1, 2015, Retrieved from the Internet: URL:http://onlinepubs.trb.org/onlinepubs/nchrp/docs/HNCHP09-58_Phl_InterimReport.pdf [retrieved on Mar. 20, 2017].
Anderson, et al. (1994) "Binder Characterization and Evaluation, vol. 3: Physical Characterization", SHRP-A-369, Strategic Highway Research Program, 4 pages.
Andrew Hanz et al., "Extended Aging of RAS Mixes with Rejuvenator", Aug. 10, 2016, Binder Expert task Group Meeting, retrieved from the Internet: URL:https://www.asphaltpavement.org/PDFs/Engineering_ETGs/Binder201609/06 Hanz Extended Aging of RAS Mixes with Rejuvenator.pdf, retrieved on Nov. 23, 2017.
Anonymous, "The Use of REOB/VTAE in Asphalt (IS-235)," Apr. 13, 2016, pp. 1-92, Retrieved from the Internet: URL:http://www.asphaltinstitute.org/wp-content/uploads/IS235_REOB_VTAE_Asphaltinstitute.pdf [retrieved on Mar. 20, 2017].
Anonymous: "Standard Test Method for Determining the Flexural Creep Stiffness of Asphalt Binder Using the Bending Beam Rheometer (BBR); ASTM D 6648-01", Aug. 1, 2001, pp. 1-14, Retrieved from the Internet: URL: ftp://185.72.26.245/Astm/1/Section04/ASTM0403/PDF/D6648.pdf, retrived on Mar. 14, 2017.
ASTM D6521-13 (2013) "Standard Practice for Accelerated Aging of Asphalt Binder Using a Pressurized Aging Vessel (PAV)", Astm International, 6 pages.
B. Holmbom et al., "Compostion of Tall Oil Pitch", Journal of the American Oil Chemist's Society, vol. 55, Feb. 23, 1978, pp. 342-344, Retrieved from the Internet: URL:http:www.springerlink.com/content/j37742625p63ggtl/fulltext.pdf [retrieved on Apr. 24, 2012].
B-Sitosterol.Powder, Supplier: MP Biomedicals, Printed from VWR Website, Date: Jun. 9, 2016, 1 page.
Cao, et al. (2011) "Chemical Structures of Swine-Manure Chars Produced under Different Carbonization Conditions Investigated by Advanced Solid-State 13C Nuclear Magnetic Resonance (NMR) Spectroscopy", Energy Fuels, 25:388-397.
Changping Sui et al., "New Low-Temperature Performance-Grading Method: Using 4-mm Parallel Plates on a Dynamic Shear Rheometer", Transportation Research Record, vol. 2207, Dec. 1, 2011.
Changping Sui et al., "New Technique for Measuring Low-Temperature Properties of Asphalt Binders with Small Amounts of Material", Transportation Research Record, Transportation Research Board, Washington, DC, US, vol. 2179, Dec. 1, 2010, pp. 23-28.
Cox, Russell Brian "Asphalt Binders Containing a Glyceride and Fatty Acid Mixture and Methods for Making and Using Same", U.S. Appl. No. 62/074,526, filed Nov. 3, 2014, 64 pages.
E.E. McSweeney et al., "Composition of Crude Tall Oil & Fractionation Products (Chapter 2)" in "Tall Oil and Its Uses-II", Jan. 1, 1987, Pulp Chemicals Association, pp. 12-19.
Endo, Yasushi (1990) "Minor Components in Edible Fats and Oils" Oil Chemistry, 39(9):611-617 (English Abstract on p. 611).
Farrar, et al. (2012) "Thin Film Oxidative Aging and low Temperature Performance Grading using Small Plate Dynamic Shear Rheometry: An Alternative to Standard RTFO, PAV, and BBR", 5th Eurasphalt & Eurobitume Congress, 10 pages.
Fini et al. (2012) "Application of Swine Manure in Development of Bio-Adhesive", Allen D. Leman Swine Conference, p. 244.
Fini, et al. (2010) "Characterization and Application of Manure-Based Bio-Binder in Asphalt Industry", Transportation Research Board 89th Annual Meeting, 14 pages.
Fini, et al. (2011) "Chemical Characterization of Biobinder from Swine Manure: Sustainable Modifier for Asphalt Binder", Journal of Materials in Civil Engineering, 23(11):1506-1513.
Fini, et al.(2011) "Application of Bio-Binder from Swine Manure in Asphalt Binder", Annual Meeting, 15 pages.
G.M. Rowe, "[Delta]Tc—Some Thoughts on the Historical Development," Binder ETG Meeting, Apr. 28, 2016, pp. 1-43, retrieved from the Internet: URL:https://www.asphaltpavement.org/PDFs/Engineering_ETGs/Binder_201604/13Rowe-DTc- Historical development.pdf [retrived on Mar. 22, 2017].
Geoffrey M. Rowe, "Asphalt Modification", 56th Illinois Bituminous Paving Conference, Dec. 15, 2015, pp. 1-42, Champaign, Illinois, USA, Retrieved from the Internet: URL:http://conferences.ict.illinois.edu/bituminousconference/56th Annual Presentations and Attendees/Rowe.pdf [retrieved on Mar. 20, 2017].
Gerald Reinke et al., "Extended Aging of RAS Mixes with Rejuvenator an Update", May 4, 2017, Binder Expert task Group Meeting, retrieved from the Internet: URL:https://www.asphaltpavement.org/PDFs/Engineering_ETGs/Binder201705/12_Reinke&Hanz_UpdateExtendedAgingofRAS.pdf, retrieved on Nov. 23, 2017.
Gerald Reinke et al., "Further Investigations Into the Impact of REOB & Paraffinic Oils on the Performance of Bitiminous Mixtures", Binder EIG Meeting, Apr. 9, 2015, pp. 1-92, Fall River, MA, USA, Retrieved from the Internet: URL:http://www.asphaltinstitute.org/wo-content/uploads/2015-April-Binder-EIG-04_Reinke_MTE-REOB-OTHER-PARAFFINIC-OILS-w-notes-w-crack-maps.pdf.
H. Takano et al., "Chemical and Biochemical Analysis Using Scanning Force Microscopy", Chem. Rev., 1999, 99, 2845-2890.
Hajime Takano et al., "Chemical and Biochemical Analysis Using Scanning Force Microscopy", Chemical Reviews, vol. 99, No. 10, Oct. 1, 1999, pp. 2845-2890.
Harhar, et al., "Chemical Characterization and Oxidative Stability of Castor Oil Grown in Morocco", Moroccan Journal of Chemistry, 4(2):279-284.
Hill, "The when, how and benefits of using thinlays for pavement preservation", 2015, Equipment World (Year: 2015). *
International Search Report and Written Opinion for International Application No. PCT/US2016/037077, dated Apr. 5, 2017, 20 pages.
International Search Report and Written Opinion for International Application No. PCT/US2016/064950, dated Apr. 19, 2017, 12 pages.
International Search Report and Written Opinion for International Application No. PCT/US2016/064961, dated Apr. 5, 2017, 23 pages.
International Search Report and Written Opinion for International Application No. PCT/US2017/045887, dated Dec. 8, 2017, 14 pages.
International Search Report and Written Opinion for International Application No. PCT/US2018/043387, dated Nov. 28, 2018, 17 pages.
International Search Report and Written Opinion for International Application No. PCT/US2018/055443, dated Jan. 31, 2019, 14 pages.
International Search Report and Written Opinion for International Application No. PCT/US2020/042202, dated Oct. 15, 2020, 24 pages.
Jarde, et al. (2007) "Using Sterols to Detect Pig Slurry Contribution to Soil Organic Matter", Water Air Soil Pollut, 178:169-178.
Kriz, et al. (2007) "Glass Transition and Phase Stability in Asphalt Binders", Road Materials and Pavements Design, 30 pages.
Logan, R.L., (Nov. 1979) "Tall Oil Fatty Acids", Journal of American Oil Chemists Society, 56:777A-779A.
Loughrin, et al. (2006) "Free Fatty Acids and Sterols in Swine Manure", Journal of Environmental Science and Health, Part B, 41:31-42.
Material Safety Data Sheet, Catalog No. 102886, Revision date: Apr. 26, 2006, Product Name: beta-Sitosterol Practical Grade, 5 pages.
Mogawer, et al. (2012) "Performance Characteristics of High Rap Bio-Modified Asphalt Mixtures", Transportation Research Board 91st Annual Meeting, 16 pages.
Muhlen, et al., Introduction to Atomic Force Microscopy and its Application to the Study of Lipid Nanoparticles , Chapter 7 in Particle and Surface Characterization Methods, ISBN 3887630572, pp. 98-127.
Product Data Sheet from MP Biomedicals Website, Catalog No. 102886, beta-Sitosterol, 1 page.
R.M. Overney et al., "Friction Measurement on Phase-Separated Thin Films with a Modified Atomic Force Microscope", Nature, Nature Publishing Group, United Kingdom, vol. 359, Sep. 10, 1992, pp. 133-135.
Reinke et al. "Investigation of Sterol Chemistry to Retard the Aging of Asphalt Binders, Transportation Research Record", TRB 2017 Annual Meeting, Jan. 1, 2017, pp. 1-13.
Richard Cantrill, Ph.D., "Phytosterols, Phytostanols and Their Esters", 2008, 13 pages.
Rossi, et al. (2017) "Adhesion Promoters in Bituminous Road Materials: A Review", Applied Sciences, 7(524):1-10.
Rubab, et al. (2011) "Effects of Engine Oil Residues on Asphalt Cement Quality", Canadian Technical Asphalt Association Conference, 12 pages.
T. Verleyen et al., "Analysis of Free and Esterified Sterols in Vegetable Oils", Journal of the American Oil Chemists Society (Jaocs), vol. 79, No. 2,Feb. 1, 2002, pp. 117-122.
T. Verleyen et al., "Influence of the Vegetable Oil Refining Process on Free and Esterified Sterols. J Am Oil Chem Soc", Article in Journal of the American Oil Chemists' Society, Sep. 2002, 8 pages.
Wakefield, Amma (Aug. 15, 2018) "ΔTc: A Parameter to Monitor Asphalt Binder's Kryptonite" Asphalt, 33(2):24-27.
Yan, et al., (2011), "Recovery of Phytosterols from Waste Residue of Soybean Oil Deodorizer Distillate", Soybean-Applications and Technology, 13 pages.
Zaumanis, et al. (2014) "Evaluation of Different Recycling Agents for Restoring Aged Asphalt Binder and Performance of 100 % Recycled Asphalt", Materials and Structures, 48(8):2475-2488.

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